Fabrication of hydrophobic, mechanically flexible and optically transparent polyimide aerogels
12365764 ยท 2025-07-22
Assignee
Inventors
- Hani NAGUIB (Toronto, CA)
- Omid AGHABABAEI TAFRESHI (Toronto, CA)
- Shahriar GHAFFARI-MOSANENZADEH (North York, CA)
- Zia SAADATNIA (North York, CA)
Cpc classification
C08G73/101
CHEMISTRY; METALLURGY
C08J2379/08
CHEMISTRY; METALLURGY
C08G73/1067
CHEMISTRY; METALLURGY
International classification
Abstract
The present disclosure provides a method of fabrication of physically crosslinked polyimide (PCPI) aerogels with significantly improved properties using no chemical crosslinker. The fabricated PCPI aerogels present high moisture resistance, hydrophobic behavior, ultralow density, ultrahigh porosity, excellent thermal stability, increased mechanical strength, and high mechanical flexibility. Also, samples have been successfully fabricated in a thin-film geometry with high mechanical flexibility and controlled thickness. Furthermore, some fabricated aerogel films present improved optical transparency of over 80%, which is the highest transparency reported so far for organic PI aerogels.
Claims
1. A polyimide aerogel, comprising: a polyimide-based polymer of the formula 1: ##STR00005## wherein n is an integer in a range between about 30 to about 50, and wherein the polymer is physically crosslinked through polymer chain entanglement, and the aerogel is formed by a process including initial gelation for about 1-10 minutes; and wherein the aerogel is free of polyamic amide polymer.
2. The polyimide aerogel according to claim 1, wherein the aerogel has a pore size in a range from about 2 nanometers to about 100 nanometers.
3. The polyimide aerogel according to claim 1, wherein the aerogel has pores with a pore size of less than about 2 nanometers.
4. The polyimide aerogel according to claim 1, wherein the aerogel has a porosity in a range from about 85% to about 99%.
5. The polyimide aerogel according to claim 1 is free of chemical crosslinkers.
6. The polyimide aerogel according to claim 1, wherein the aerogel has a density in a range from about 0.07 g/cm.sup.3 to about 0.25 g/cm.sup.3.
7. The polyimide aerogel according to claim 1, wherein the aerogel has a thermal conductivity in a range from about 15 to about 50 milliwatts/degrees Kelvin-meters.
8. The polyimide aerogel according to claim 1, wherein the aerogel is characterized by a hydrophobicity in a range from about 90 degrees to about 140 degrees water contact angle.
9. The polyimide aerogel according to claim 1, wherein the aerogel is characterized by a water uptake as low as about 1%.
10. The polyimide aerogel according to claim 1, wherein the aerogel has an onset of thermal decomposition in a range from about 500 to about 700 C.
11. The polyimide aerogel according to claim 1, wherein the aerogel has a dielectric constant in a range from about 1.5 to about 3.
12. The polyimide aerogel according to claim 1, wherein the aerogel is in the form of a film having a thickness of at least about 80 microns, and wherein the aerogel has optical transparency in a range from about 60% to about 99%.
13. The polyimide aerogel according to claim 1, wherein the aerogel is characterized by a compressive modulus in a range from about 17 to 25 Mega Pascal (MPa).
14. The polyimide aerogel according to claim 1, wherein the aerogel is characterized by a tensile modulus in a range from about 1 to 5 Mega Pascal (MPa).
15. A process of making a polyimide aerogel of claim 1, comprising the steps of forming a wet gel by reacting a diamine monomer (DIAM) with a dianhydride monomer (DIAH) in a reaction solution comprising a dipolar aprotic solvent to form the polymer of Formula A; wherein n is between the range of 30 to 50 ##STR00006## imidizing the formed polymer; gelation of the formed polymer for about 1-10 minutes; replacing the aprotic solvent with a drying solvent; and removing the drying solvent from the formed wet gel.
16. The process of claim 15, wherein the step of imidizing the formed polymer is performed through thermal imidization or chemical imidization.
17. The process of claim 15, further comprising the step of aging the wet gel obtained by the initial gelation to increase the polymerization yield and to advance the degree of physical crosslinking.
18. The process of claim 15, wherein the aprotic solvent is N-methylpyrrolidinone (NMP), dimethylformamide (DMF), dimethyl sulfoxide (DMSO), or a mixture of NMP and tetrahydrofuran (THF).
19. The process of claim 15, wherein the step of reacting the DIAM monomer with the DIAH monomer is done without the use of a chemical crosslinker.
20. The process of claim 15, wherein the DIAM monomer and DIAH monomer are first dissolved separately then the DIAM monomer solution is combined with the DIAH monomer solution.
21. The process of claim 15, wherein DIAM monomer is first dissolved and DIAH monomer is added to the DIAM solution.
22. The process of claim 15, wherein the diamine monomer (DIAM) is 2,2-dimethylbenzidine (DMBZ).
23. The process of claim 15, wherein the dianhydride monomer (DIAH) is biphenyl-tetracarboxylic acid dianhydride (BPDA).
24. The process of claim 15, wherein the drying solvent is removed via supercritical drying, freeze drying, or ambient pressure drying.
25. The process of claim 15, wherein the wet gel forming step occurs over a period of time ranging between about 1 minute to about 24 hours.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The disclosure will be more fully understood from the following detailed description thereof taken in connection with the accompanying drawings, which form part of this application, and in which:
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DETAILED DESCRIPTION
(23) The synthesis of hydrophobic, mechanically flexible, and optically transparent polyimide aerogels is disclosed herein. Although embodiments of the present invention are disclosed herein, the disclosed embodiments are merely exemplary and it should be understood that the invention relates to many alternative forms, including different shapes and sizes. Furthermore, the Figures are not drawn to scale and some features may be exaggerated or minimized to show details of particular features while related elements may have been eliminated to prevent obscuring novel aspects. Therefore, specific structural and functional details disclosed herein are not to be interpreted as limiting but merely as a basis for the claims and as a representative basis for enabling someone skilled in the art to employ the present invention in a variety of manners.
(24) As used herein, the terms comprises, comprising, includes and including are to be construed as being inclusive and open-ended, and not exclusive. Specifically, when used in this specification including claims, the terms comprises, comprising, includes and including and variations thereof mean the specified features, steps, or components are included. These terms are not to be interpreted to exclude the presence of other features, steps, or components.
(25) As used herein, the terms about and approximately, when used in conjunction with ranges of dimensions, compositions of mixtures, or other physical properties or characteristics, are meant to cover slight variations that may exist in the upper and lower limits of the ranges of dimensions so as to not exclude embodiments where on average most of the dimensions are satisfied but where statistically dimensions may exist outside this region. It is not the intention to exclude embodiments such as these from the present invention.
(26) As used herein, the coordinating conjunction and/or is meant to be a selection between a logical disjunction and a logical conjunction of the adjacent words, phrases, or clauses. Specifically, the phrase X and/or Y is meant to be interpreted as one or both of X and Y wherein X and Y are any word, phrase, or clause.
(27) As used herein, the phrase physical crosslinking refers to intermolecular bonds or interactions between polymer chains without involving any chemical reactions, in this mechanism the polymer chains network is held together by entanglements due to long polymer chains with high molecular weights as well as various weak forces, such as van der Waals forces, hydrogen bonding, or dipole-dipole interactions.
(28) Conversely, chemical crosslinking refers to chemical bonds being formed between the polymer chains by covalent bonds and typically requires the use of specific chemical agents. Chemical cross linkers may be selected from the group consisting of a triamine, an aliphatic amine comprising three or more amines, an aliphatic triamine, an aromatic amine comprising three or more amine groups, an aromatic triamine, 1,3,5-tri(aminophenoxy)benzene, a silica gel structure decorated with three or more amines, to give some non-limiting examples.
(29) As used herein, the phrase aerogel refers to a class of mesoporous solid materials with an open-cell structure where the average pore size ranges from about 2 to about 50 nm, made by removing the liquid content of the wet gels while the solid network remains intact.
(30) As used herein, the phrase diamine refers to a type of polyamine with exactly 2 amino groups. In addition to the diamine used in the non-limiting example below, others include, but are not limited to, 1. m-Phenylene diamine (m-PDA), 2. p-Phenylene diamine (p-PDA), 3,4,4-Methylene dianiline (MDA) and 4,4,4-Oxydianiline (ODA) The present disclosure will now be illustrated with the following non-limiting example.
EXPERIMENTAL
(31) Materials
(32) 2,2-Dimethylbenzidine (DMBZ) and biphenyl-tetracarboxylic acid dianhydride (BPDA) were selected as diamine and dianhydride monomers respectively. In our previous study [11], the DMBZ-BPDA combination was identified as the promising backbone chemistry for the fabrication of aerogels with improved moisture resistance, mechanical strength, along with thermal stability. Yet, chemically crosslinked DMBZ-BPDA are reported with highly rigid behavior and as a result low mechanical flexibility [1]. N-methylpyrrolidinone (NMP) was selected as the solvent due to its high basic aprotic nature. To catalyze the imidization reaction and scavenge water by-product of the condensation reaction, pyridine and acetic anhydride were utilized respectively. For chemically crosslinked aerogels, 1,3,5-Tris(4-aminophenyl)benzene (TAPB) was selected as the crosslinking agent. Ethyl alcohol 100% was used in the solvent exchange step. All reagents were purchased from Sigma Aldrich and were used without further purification.
(33) Characterization
(34) The density of aerogels was measured using a caliper and an electronic scale. By comparing the retained diameter and the initial diameter of aerogels, the shrinkage was calculated. The helium pycnometer (Quantachrome Instrument Ultra-Foam 1000) was utilized in accordance with the ASTM D6226 standard to measure the porosity of samples. The electronic microscope (Field Emission SEM, Quanta, model FEG-250) was operated at 5-15 kV to assess the morphological features of the samples. Using a Perkin Elmer Spectrum, Fourier transient infrared (FTIR) was performed on PCPI aerogels to identify their chemical structures through measuring spectral transmittance and evaluation of chemical bonds. A spectral range of 4000-650 cm.sup.1 was used for spectra transmittance collection with a spectral resolution of 4 cm.sup.1.
(35) In order to characterize the surface wetting of PCPI aerogels, a contact angle goniometer was utilized (Ossila Contact Angle Goniometer L2004A1). Using a micropipette, a water droplet was suspended on the surface of samples, and using analytical software, captured images were analyzed and WCA was recorded. Further wettability analysis was performed to assess the water uptake capability of aerogels. Similar to the previously reported methodology [12], the prepared samples were fully immersed in distilled (DI) water at 25 C. and allowed to soak for 24 hours. Then, in order to remove excess water, wet samples were wiped, and using the scale, their weights were evaluated. The water uptake of aerogels was measured using Eq. (1):
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here W.sub.i and W.sub.f are the initial (before the test) and final (after the test) weights of samples respectively.
(37) To analyze the thermal stability and obtain the onset of decomposition of aerogels, thermo-gravimetric analysis (TGA) was performed on a TA-Instrument Q50. Under the nitrogen environment, the temperature was increased from 25 to 700 C. at the rate of 10 C. min.sup.1, and sample weight loss was monitored. Compressive properties of monolith aerogels, including compressive modulus and strength, were evaluated based on D695-02a ASTM guidelines. Instron 5848 micro-tester was used for this purpose. All compression tests were performed at the rate of 0.05 in min.sup.1. Moreover, a Dynamic Mechanical Analyzer (DMA, Q800, TA Instrument) was used for the tensile strength test. The dielectric constant of aerogels was measured using an Alpha-A high-performance conductivity analyzer (Novocontrol Technologies GmbH & Co. KG, Germany) and measurements were performed in the frequency range of 10.sup.1-10.sup.5 Hz. The optical properties of samples (transmittance and haze) were measured using the PerkinElmer Lambda 1050 UV-Vis spectrophotometer with a 150 mm integrating sphere in the spectral range of 200-2500 nm.
(38) Preparation of Physically Crosslinked Polyimide Aerogels
(39) The preliminary studies we performed suggested the prominent role of monomers' reaction time in the formation of a highly viscous polyamic acid (PAA) precursor, leading to the physically crosslinked PI aerogels. At 14 wt % solid/solvent and the number of the repeat unit of 35 (n=35), when the diamine (DMBZ) was dissolved in NMP (in 30 min) and the dianhydride (BPDA) was added into the solution, upon 2 h monomers' reaction, it was observed that the PAA reached high viscosity, enabling the formation of a gel network even in the absence of a chemical crosslinker (PCPI-1). Subsequently, in an attempt to improve the monomers' quality of dispersion, both DMBZ and BPDA were dissolved separately in 50% NMP. A parametric study was accordingly designed to evaluate the significance of monomers' dispersion time, along with the diamine-dianhydride reacting strategy, to fully understand the contribution of processing parameters in the formation of PCPI aerogels (see Table 1).
(40) TABLE-US-00001 TABLE 1 Samples' material composition and processing details n (repeat Solid/Solvent Reaction Sample Diamine Dianhydride units) (wt %) Time Fabrication Process PCPI-1 DMBZ BPDA 35 14 2 h DMBZ in 100% NMP 30 min, add BPDA 10 min PCPI-2 DMBZ BPDA 35 14 20 min DMBZ & BPDA each in 50% NMP 30 min, mix PCPI-3 DMBZ BPDA 35 14 20 min DMBZ & BPDA each in 50% NMP 60 min, mix PCPI-4 DMBZ BPDA 35 14 20 min DMBZ & BPDA each in 50% NMP 24 h, mix PCPI-5 DMBZ BPDA 35 14 2 h DMBZ & BPDA dissolved 60 min, 20 min mix & 100 min ageing PCPI-6 DMBZ BPDA 35 14 2 h DMBZ & BPDA in 50% NMP 60 min, mix 200 rpm PCPI-7 DMBZ BPDA (TAPB) 35 14 30 min DMBZ & BPDA each in 50% NMP 60 min, mix CCPI DMBZ BPDA (TAPB) 35 7.5 2 h DMBZ & BPDA each in 50% NMP 60 min, mix
(41) As an example, formulation PCPI-6 from Table 1, consisting of 15.8 mmol % DMBZ and 16.25 mmol % BPDA at 14 wt % solid/solvent and n=35, was prepared as follows (illustrated in
(42) As can be observed from
Results and Discussion
(43) Density, Shrinkage, and Porosity
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(46) In reaction with the BPDA dianhydride monomer, the rigid DMBZ diamine is known to result in higher porosity compared to the other diamines such as PPDA and ODA [[3]]. Compared to the chemically crosslinked PI aerogels, the fabricated PCPI aerogels presented even higher porosity with the observed porosity ranging from 95.09% to 98.46%. High porosity will be beneficial in improving a wide range of aerogel properties including but not limited to reduced weight, increased filtration efficiency, and enhanced thermal insulation performance.
(47) From the previous works on chemically crosslinked PI aerogels, density is increased with increasing the number of repeat units and higher molecular weight [1], [8]. Based on this trend, the increased density of the fabricated PCPI aerogels at higher porosity may suggest the greater molecular weight of the fabricated PCPI aerogels compared to chemically crosslinked counterparts. Such high molecular weight and as a result longer polymer chains is the key component of the crosslinking of PCPI samples without using chemical crosslinkers.
(48) Aerogel Morphology
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(50) This observation agrees with the porosity and density trend of the PCPI-1, PCPI-2, and PCPI-3 samples. As observed from
(51) Based on the significantly faster initiation time of the physical crosslinking mechanism (1-4 min) compared to the required time for gelation using the TAPB chemical crosslinker (0.5 to 1 h), the main crosslinking and gelation mechanism in PCPI-7 is still expected to be the physical. Yet, as presented in
(52) Chemical Structures
(53) The FTIR was carried out to identify the main characteristic bands and functional groups along with validating the successful imidization of PCPI aerogels. Looking at the FTIR results presented in
(54) Hydrophobicity and Moisture Resistance
(55) The wettability properties of PCPI aerogels were evaluated through the measurement of water uptake along with the water contact angle (WCA) to shed light on the hydrophobicity and moisture resistance of prepared aerogels. Our previous studies showed that pristine PI aerogels synthesized via the chemical crosslinking route exhibited super hydrophilicity resulting from the polar structures of PI; therefore the resultant PI aerogels cannot be employed in moisture-sensitive environments. In this work, in an attempt to assess the moisture resistance of fabricated PCPI aerogels, the water uptake test was carried out in which by comparing the weight of samples before and after the test, the water uptake ratio of samples was calculated.
(56) As can be observed in
(57) Surprisingly, PCPI-6 exhibited an ultralow water uptake of 15%, considerably lower than previously reported PI aerogels including poly(maleic anhydride) crosslinked PI aerogels (up to 700%) [13], bis(trimethoxysilylpropyl)amine (BTMSPA) crosslinked ODA-BPDA aerogels (up to 500%) [14], and 1,3,5-Triaminophenoxybenzene (TAB) crosslinked ODA-BPDA aerogels (up to 383%) [15]. The excellent moisture resistance of PCPI-6 was also comparable to other chemically-modified PI aerogels namely the ones with the incorporation of 1,12-dodecyldiamine (DADD) [16], 2,2-bis(3,4-dicarboxyphenyl)hexafluoropropane dianhydride (6FAPB) [15], and 2,2-Bis [4-(4-aMinophenoxy) phenyl]propane (BAPP) [14]. Benefiting from its low ultralow water uptake, PCPI-6 showed the ability to maintain its physical structure during the test and did not collapse which could be due to the strong physical crosslinking of the aerogel network.
(58) To better understand the moisture-resistant behavior and ultralow water uptake of PCPI-6, contributing factors in the process of water absorption in PI aerogels should be discussed first. One major factor is the hydrophobicity/hydrophilicity of the polymer chains which must be considered. When the polymeric backbone contains O (like the one in ODA), it is more likely that the resultant PI aerogels will be susceptible to moisture as was observed in previous studies. In contrast to ODA structure, DMBZ was reported to improve hydrophobicity which is due to its chemical structure. In general, to characterize the wettability of the surface, WCA is measured. The WCA of over 90 indicates the fact that wetting of the surface is unfavorable.
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(60) Another influential factor is the morphological characteristic of aerogels including crosslinking degree and the mesoporous structure. It is well known that the aerogel pore size and pore structure have a considerable impact on their water uptake. As explained by Guo et al. [13], aerogels with larger pore sizes allow water in more easily resulting in higher water uptake. This phenomenon was not only observed in PI aerogels, but it applies to other aerogels e.g. cellulose-based aerogels [17]. Further and even more importantly, though, the physical crosslinking of PCPI aerogels played a critical role in their moisture-resistant capability. With the application of mechanical mixing in the fabrication of PCPI-6, the physical crosslinking of the wet gel network was strengthened and along with the higher degree of entanglements, a decrease in water uptake resulted. Moreover, observation of similar hydrophobic behavior from smaller cuts of the samples presented that the moisture resistance of the fabricated aerogels is not due to their surface (skin) properties.
(61) Thermal Stability
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(64) As seen in
(65) Electrical Properties
(66) Due to the nano-sized structure and highly porous network of aerogels, they typically exhibit ultralow dielectric constants, which are desirable for applications like microelectronics, antennas, and microwave circuitry. In this study, in order to measure the dielectric constant of prepared PCPI aerogels, an Alpha-A high-performance conductivity analyzer was employed. All aerogel samples were equilibrated at atmospheric conditions, and the dielectric permittivity measurement was carried out at 298 K for the frequency range of 10.sup.1-10.sup.5 Hz. Both the real part (also known as dielectric constant) and the imaginary part (also known as loss factor) were measured. The dielectric constants of PCPI aerogels at varied frequencies are shown in
(67) In general, it is known that the dielectric constant of aerogels is dominated by the chemical backbone structure, and more importantly the free volume fraction of the aerogel network (i.e., degree of porosity). Based on this principle, for PCPI-1 to PCPI-6 samples with similar compositions, it can be fairly suggested that the dielectric constant is closely related to their porosity (or density), the lower the density, the higher the porosity, and the lower the dielectric constant. Such a relation is depicted in
(68) Mechanical Properties
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(70) The compressive modulus and strength of PCPI aerogels were characterized using mechanical compression tests based on ASTM D695-02a. The cylindrical aerogels were subjected to compressive stress at the rate of 0.05 in min.sup.1, and upon monitoring stress-strain curves, modulus E.sub.c (initial slope of the curve) and strength (yield point achieved after linear elastic region) were recorded. Looking at stress-strain curves in
(71) The synthesis strategy disclosed herein has also promoted the elastic modulus of developed aerogels compared to other PI aerogels. Such an enhancement is highlighted in
(72) For all compositions listed in Table 1, thin-film PCPI aerogels can also be fabricated using the film-casting method. As shown in
(73) In fact, the development of flexible thin-film aerogels with improved thermal and mechanical properties using facile strategies has been a longstanding challenge. Although in the past few years, flexible aerogel films based on graphene, cellulose, silica, and even PI have been reported, they are either complicated to prepare or limited for large-scale production due to their high costs. In this context, the development of more cost-effective and facile strategies, such as the one proposed in this study, can be of great interest to further extend the application of PI aerogels in practical fields namely aerospace, insulation of buildings, microelectronics, and even winter clothing.
(74) Typical stress-strain curves of PCPI aerogel films from tensile tests are shown in
(75) Optical Transparency
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(77) For selected PCPI aerogel films, light transparency was measured using a UV-Vis spectrophotometer by placing the samples over the integrating sphere transmittance port. Light transparency of aerogel films, along with their corresponding density, are demonstrated in
(78) The improved transparency of PCPI aerogel films in this work compared to reported PI aerogels can be due to the employment of a physical crosslinking strategy and the elimination of the crosslinking agent. Along with slightly different chemical compositions and molecular weight, all these resulted in enhanced transparency. Furthermore, a more uniform and smaller pore-size distribution could have also caused such high transparency. Another important factor that was rarely discussed in the literature is the aerogel film's thickness. This is of high importance from the application point of view, especially when thermal insulation performance is needed.
(79) As presented in
(80) However, for aerogels with smaller particle sizes, such a dependency became minimal, and high transparency was maintained at various thicknesses. However, the facts behind the light transparency of aerogels are still not fully clear, and other sample parameters namely density, molecular weight, and chain packing ability may also play an active role, and further research needs to be conducted. Eventually, it should be noted that not all aerogels can be made into thin-film configurations with controlled thickness while maintaining their mechanical flexibility. For instance, silica aerogels due to their inherent brittleness do not have the capability to be transformed into thin-film aerogels without structural disintegration. Therefore, it can be argued that the physical crosslinking route introduced in this study can have great potential in the fabrication of thin-film aerogels (which are essential for conformable applications) with controlled thickness and tailored properties.
(81) In an embodiment, the present disclosure provides a polyimide aerogel, comprising: a polyimide-based polymer of the formula 1:
(82) ##STR00003##
wherein n is an integer in a range between about 30 to about 50, and wherein the polymer is physically crosslinked through polymer chain entanglement.
(83) In embodiments, the aerogel has a pore size in a range from about 2 nanometers to about 100 nanometers, or a pore size in a range from about 2 nanometers to about 50 nanometers, or the pore size is less than about 2 nanometers.
(84) In embodiments, the aerogel has a porosity in a range from about 85% to about 99%, or the porosity is in a range from about 95% to about 99%.
(85) In embodiments, the aerogel is free of chemical crosslinkers.
(86) In embodiments, the aerogel has a density in a range from about 0.07 g/cm.sup.3 to about 0.25 gm/cm.sup.3.
(87) In embodiments, the aerogel has a thermal conductivity in a range from about 15 to about 50 milliwatts/degrees Kelvin-meters.
(88) In embodiments, the aerogel is characterized by a hydrophobicity in a range from about 90 degrees to 140 degrees water contact. angle.
(89) In embodiments, the aerogel is characterized by a water uptake as low as about 1%.
(90) In embodiments, the aerogel has an onset of thermal decomposition in a range from about 500 to 700 C.
(91) In embodiments, the aerogel has a dielectric constant in a range from about 1.5 to 3.
(92) In embodiments, the aerogel is in the form of a film having a thickness of at least about 80 microns.
(93) In embodiments, the aerogel has an optical transparency in a range from about 60% to about 99%.
(94) In embodiments, the aerogel is characterized by a compressive modulus in a range from about 17 to 25 Mega Pascal (MPa).
(95) In embodiments, the aerogel is characterized by a tensile modulus in a range from about 1 to 5 Mega Pascal (MPa).
(96) In embodiments there is provided a process of making a polyimide aerogel comprising the steps of: forming a wet gel by reacting a diamine monomer (DIAM) with a dianhydride monomer (DIAH) in a reaction solution comprising a dipolar aprotic solvent to form the polymer of Formula A; wherein n is between the range of 30 to 50
(97) ##STR00004## imidizing the formed polymer; replacing the aprotic solvent with a drying solvent; and removing the drying solvent from the formed wet gel.
(98) In embodiments of the process, other diamines and dianhydrides may work. However, the properties including the hydrophobicity and mechanical properties could be different ones as below, for example, non-limiting alternatives to DIAM include m-Phenylene diamine (m-PDA), p-Phenylene diamine (p-PDA), 4,4-Methylene dianiline (MDA) and 4,4-Oxydianiline (ODA).
(99) In embodiments, alternatives to DIAH include, but are not limited to, Pyromellitic dianhydride (PMDA), 2,2-Bis(3,4dicarboxyphenyl)hexafluoropropane dianhydride (6FDA), 2,2-Bis[4-(3,4dicarboxyphenoxy)phenyl]propane-dianhydride (BPADA), Benzophenonetetracarboxylic dianhydride (BTDA), and 4,4-Oxydiphthalic anhydride (ODPA).
(100) In an embodiment, the step of imidizing the formed polymer is performed through thermal imidization or chemical imidization. Thermal imidization is not a usual imidization process for PI aerogels due to the fact that it needs a temperature of up to 300 degrees Celsius which may result in solvent evaporation and significant shrinkage. However, thermal imidization can be done either after super-critical drying when the solvent is already extracted, or by heating using a pressure vessel to avoid solvent evaporation, which is a more complicated process.
(101) In an embodiment, the step of imidizing is performed via chemical imidization.
(102) In an embodiment, the chemical imidization is done by adding a chemical dehydrating agent to the reaction solution.
(103) In an embodiment, the chemical dehydrating agent may be a mixture of an alkanoic anhydride and an organic base. The alkanoic anhydrides may comprise acetic anhydride, propionic anhydride, benzoic anhydride, n-butyric anhydride, trifluoroacetic anhydride or any combination thereof. The organic base may comprise pyridines, mono-, di- and trialkyl amines, isoquinoline, piperazine, morpholine, piperidine, or any combination thereof.
(104) In an embodiment, the chemical dehydrating agent is a mixture of acetic anhydride and pyridine.
(105) In an embodiment, the process includes a step of quick gelation and aging the wet gel to increase the polymerization yield and to advance the degree of physical crosslinking. Physical crosslinking is done by physical entanglement of the formed polymer chains and can be described morphologically. However, with respect to the very small size of polymer chains, tens of nanometers, calculating the degree of physical crosslinking using image processing will be challenging. Yet, it is still possible to compare the properties of different physically crosslinked aerogels, such as mechanical, to compare their degree of crosslinking.
(106) In an embodiment, the quick gelation occurs for a period of time ranging between 1 minute to 10 minutes.
(107) In an embodiment, the aging of the wet gel is done for a period of time ranging between 90 minutes and 48 hours.
(108) In an embodiment, the aprotic solvent is N-methylpyrrolidinone (NMP), dimethylformamide (DMF), dimethyl sulfoxide (DMSO), or a mixture of NMP and tetrahydrofuran (THF).
(109) In an embodiment, the process includes a step of adding a chemical crosslinker to the reaction solution. Non-limiting examples of chemical crosslinkers include a triamine, an aliphatic amine comprising three or more amines, an aliphatic triamine, an aromatic amine comprising three or more amine groups, an aromatic triamine, 1,3,5-tri(aminophenoxy)benzene, a silica gel structure decorated with three or more amines.
(110) In an embodiment, the step of reacting the DIAM monomer with the DIAH monomer is done without the use of a chemical crosslinker.
(111) In an embodiment, the DIAM monomer and DIAH monomer are first dissolved separately then the DIAM monomer solution is combined with the DIAH monomer solution.
(112) In an embodiment the DIAM monomer is first dissolved and the DIAH monomer is added to the DIAM solution.
(113) In an embodiment, the aprotic solvent is N-methylpyrrolidinone (NMP).
(114) In an embodiment, the diamine monomer (DIAM) is 2,2-dimethylbenzidine (DMBZ).
(115) In an embodiment, the dianhydride monomer (DIAH) is biphenyl-tetracarboxylic acid dianhydride (BPDA).
(116) In an embodiment, the drying solvent is removed via supercritical drying, freeze drying, or ambient pressure drying.
(117) In an embodiment, the drying solvent is a solvent that is soluble in liquid CO.sub.2 and can be any one or combination of ethanol, acetone, toluene, tetrahydrofuran (THF), cyclohexane, or a combination thereof.
(118) In an embodiment the drying solvent is removed via freeze drying and the drying solvent is water or alcohol.
(119) In an embodiment, the drying solvent is removed via ambient drying.
(120) In an embodiment, the drying solvent is an alcohol or acetone.
(121) In an embodiment, the wet gel forming step occurs over a period of time ranging between 1 min to 24 h.
(122) In an embodiment, the process further includes a step of pouring the reacting solution into a bulk monolithic mold or a thin film mold.
(123) In an embodiment, the process further includes the step of adding an additive to the reaction solution. In an embodiment, the additive is a polymer stabilizer, a functionalizing agent, or a combination thereof, other polymers, other aerogels, carbon nanotubes, metallic fillers or particles, organic or inorganic fibers, organic or inorganic fillers or particles, or non-woven or woven fiber reinforcement composed of a carbon precursor fiber, a glass fiber, a polymeric organic fiber, a ceramic fiber, or a biopolymer fiber.
(124) In an embodiment, the additive is selected from the group consisting of polymer, aerogel, carbon nanotubes, metallic fillers or particles, organic or inorganic fibers, organic or inorganic fillers or particles, non-woven or woven fiber reinforcement composed of a carbon precursor fiber, a glass fiber, a polymeric organic fiber, a ceramic fiber, a biopolymer fiber or any combination thereof.
CONCLUSIONS
(125) PI aerogels as an important class of organic aerogels have drawn great attention in the past decade in both academia and industry. This is due to their outstanding mechanical, thermal, and chemical performance. Recently, many attempts have been is performed to tailor PI aerogels' properties mainly through changing monomers' compositions or altering chemical crosslinker type. One major shortcoming of PI aerogels, however, is the high cost and environmental impacts of chemical crosslinkers. In this study, for the first time, the present inventors have introduced the novel physical crosslinking route for PI aerogels synthesis by effectively controlling the process parameters including monomers dispersion time and reaction time. Compared to the chemically crosslinked PI aerogels, the fabricated physically crosslinked aerogels presented even higher porosity with the observed porosity ranging from 95.09% to 98.46%. Morphological characterization of PCPI aerogels showed that due to their longer monomers dissolving time and longer reaction time, physically entangled fibers with increased fiber aspect ratio and reduced fiber thickness were formed. Such a strong physically crosslinked network showed to have a noticeable impact on the mechanical properties of PCPI aerogels.
(126) A compressive modulus of over 20 MPa was obtained, which was significantly larger than the reported one in state-of-the-art PI aerogels. Interestingly, PCPI aerogels displayed outstanding moisture resistance. When the samples were fully immersed in water, water uptake as low as 15% was achieved with a WCA of over 110. Considering the fact that super hydrophilicity has been a longstanding shortcoming of PI aerogels, this work can pave the way toward the fabrication of moisture-resistant PI aerogels without sacrificing other properties. Investigation of the thermal and electrical properties of PCPI aerogels supported this phenomenon. As observed from TGA results, samples had excellent thermal stability with a decomposition temperature of about 530 C. Furthermore, the dielectric constant remained in the low range of 2.3-2.8, comparable to other low dielectric polymers.
(127) The present method is very advantageous in that the chemical formulation is fabricated using industrially available monomers of polyimide at comparable prices to polyimide foams per unit of weight. However, with respect to about 5 to 10 times lower density of fabricated material compared to polymeric foams, the material cost is expected to be significantly lower per unit of volume. Moreover, unlike previously introduced polyimide aerogels, one novelty of the introduced material is in avoiding any chemical crosslinker, those are both very expensive, as high as $80/g, and are environmentally unfriendly materials. Except for the chemical backbone materials and the chemical reagents, the processing solvents including the liquid CO.sub.2 of the drying process could be reused in a filtered circulation process. The fabrication process disclosed herein consists of simple solution mixing and casting with relatively quick gelation followed by CO.sub.2 supercritical drying. Furthermore, relatively fast gelation and thin film geometry mean simple scale-up with respect to target application requirements.
(128) Another advantage is that organic aerogels can be recycled via different methods including (i) pyrolysis (conversion of aerogels into oil and fuels through thermal degradation; (ii) solvent extraction (using aqueous or non-aqueous media for dissolving aerogels and recovering valuable components; and (iii) mechanical grinding (reusing aerogel powders in a series of consecutive procedures as absorbent for oil/chemical cleanup and insulation purposes.
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