Next Article in Journal
Compressive Mechanical Behavior and Corresponding Failure Mechanism of Polymethacrylimide Foam Induced by Thermo-Mechanical Coupling
Next Article in Special Issue
Facile Preparation of a Transparent, Self-Healing, and Recyclable Polysiloxane Elastomer Based on a Dynamic Imine and Boroxine Bond
Previous Article in Journal
Method Development for the Prediction of Melt Quality in the Extrusion Process
Previous Article in Special Issue
Poly(ester imide)s with Low Linear Coefficients of Thermal Expansion and Low Water Uptake (VII): A Strategy to Achieve Ultra-Low Dissipation Factors at 10 GHz
 
 
Search for Articles:
Title / Keyword
Author / Affiliation / Email
Journal
Article Type
 
 
Advanced Search
 
Section
Special Issue
Volume
Issue
Number
Page
 
Journals
Polymers
Volume 16
Issue 9
10.3390/polym16091198
polymers-logo
Submit to this Journal Review for this Journal Propose a Special Issue
► Article Menu

Article Menu

share Share announcement Help format_quote Cite question_answer Discuss in SciProfiles thumb_up
...
Endorse textsms
...
Comment
first_page
settings
Order Article Reprints
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Article

Intrinsically Microporous Polyimides Derived from 2,2′-Dibromo-4,4′,5,5′-bipohenyltetracarboxylic Dianhydride for Gas Separation Membranes

by
Yongle Li
1,2,
Yao Lu
3,
Chun Tian
1,*,
Zhen Wang
1 and
Jingling Yan
1
1
Ningbo Institute of Material Technology & Engineering, Chinese Academy of Sciences, Ningbo 315201, China
2
College of Chemical Engineering, Zhejiang University of Technology, Hangzhou 310014, China
3
School of Fine Arts, Zhengzhou University, Zhengzhou 450001, China
*
Author to whom correspondence should be addressed.
Polymers 2024, 16(9), 1198; https://doi.org/10.3390/polym16091198
Submission received: 22 March 2024 / Revised: 17 April 2024 / Accepted: 22 April 2024 / Published: 25 April 2024
(This article belongs to the Special Issue Advances in High-Performance Polymer Materials)
Browse Figures
Versions Notes

Abstract

:
This work aims to expand the structure–property relationships of bromo-containing polyimides and the influence of bromine atoms on the gas separation properties of such materials. A series of intrinsically microporous polyimides were synthesized from 2,2′-dibromo-4,4′,5,5′-bipohenyltetracarboxylic dianhydride (Br-BPDA) and five bulky diamines, (7,7′-(mesitylmethylene)bis(8-methyldibenzo[b,e][1,4]dioxin-2-amine) (MMBMA), 7,7′-(Mesitylmethylene)bis(1,8-dimethyldibenzo[b,e][1,4] dioxin-2-amine) (MMBDA), 4,10-dimethyl-6H,12H-5,11-methanodibenzo[b,f][1,5]diazocine-2,8-diamine (TBDA1), 4,10-dimethyl-6H,12H-5,11-methanodibenzo[b,f][1,5]diazocine-3,9-diamine (TBDA2), and (9R,10R)-9,10-dihydro-9,10-[1,2]benzenoanthracene-2,6-diamine (DAT). The Br-BPDA-derived polyimides exhibited excellent solubility, high thermal stability, and good mechanical properties, with their tensile strength and modulus being 59.2–109.3 MPa and 1.8–2.2 GPa, respectively. The fractional free volumes (FFVs) and surface areas (SBET) of the Br-BPDA-derived polyimides were in the range of 0.169–0.216 and 211–342 m2 g−1, following the order of MMBDA > MMBMA > TBDA2 > DAT > TBDA1, wherein the Br-BPDA-MMBDA exhibited the highest SBET and FFV and thus highest CO2 permeability of 724.5 Barrer. Moreover, Br-BPDA-DAT displayed the best gas separation performance, with CO2, H2, O2, N2, and CH4 permeabilities of 349.8, 384.4, 69.8, 16.3, and 19.7 Barrer, and H2/N2 selectivity of 21.4. This can be ascribed to the ultra-micropores (<0.7 nm) caused by the high rigidity of Br-BPDA-DAT. In addition, all the bromo-containing polymers of intrinsic microporosity membranes exhibited excellent resistance to physical ageing.

Graphical Abstract

1. Introduction

Polyimides (PIs) have been considered as one of the most attractive and promising gas separation membrane materials due to their good film-forming properties, excellent heat and chemical resistance, good mechanical properties, and high gas perm-selectivity. Commercial polyimides for gas separation membranes include Matrimid®5218, P84®, Upilex®, etc. [1]. However, the traditional PIs exhibit dense chain packing, resulting in a low fractional free volume (FFV) and insufficient gas permeability. Thus, their gas separation performances were below the Robeson’s upper bounds [2,3,4].
So far, there have been several emerging polymers that possess enhanced gas permeability, e.g., the polymers of intrinsic microporosity (PIMs) [5,6,7]. The excellent gas separation performance of PIMs can be explained by their twisted and highly inflexible polymer backbones, which leads to the formation of unique micropores of <2 nm and ultra-micropores of <0.7 nm [8,9]. Various PIMs have been exploited to increase polymer rigidity by incorporating bulky and stiff moieties [10], such as spirobisindane (SBI) [11], Tröger’s base (TB) [12], and triptycene (Trip) [13]. The introduction of micropores into PIs enhanced gas permeability, although a decrease in selectivity was often observed. Many PIMs have overcome the trade-off relationship and surpassed the Robeson’s upper bounds [4,14,15]. Nonetheless, PIMs still suffer several disadvantages, such as a complicated synthetic procedure, an extremely high cost, inferior mechanical properties, and poor resistance to physical ageing and CO2-induced plasticization. These limitations hamper their widespread application in gas separation [11,16,17,18]. In addition, nanoparticles were also introduced into PIMs, which can also improve the CO2 diffusion coefficients of the membranes, thereby enhancing the separation performance [19,20,21].
At present, 3,3′,4,4′-biphenyltetracarboxylic dianhydride (4,4′-BPDA) is an extensively used commercial monomer for high-performance PIs. 4,4′-BPDA-derived PIs often exhibit strong intramolecular or intermolecular interactions, such as π-π stacking, which cause high gas selectivity [22]. Tanaka et al. investigated the gas separation performance of polyimides prepared from 4,4′-BPDA and 4,4′-oxydianiline (ODA). The results showed that 4,4′-BPDA-ODA displayed a H2/CH4 and CO2/CH4 selectivity of 173 and 29, respectively [23]. However, 4,4′-BPDA-derived PIs showed relatively low gas permeability, which is attributed to strong intermolecular interactions leading to low d-spacing of the resulting polymers. This limitation can be addressed by the incorporation of bulky 2,2′-positioned substituents in 4,4′-BPDA, which can increase the d-spacing and FFV of the resulting polymers. Li et al. reported a series of PIs derived from 2,2′-disubstituted BPDAs [24,25]. The introduction of bulky substituents at the 2,2′ positions of 4,4′-BPDA restricted the rotation of the single bonds between two phthalimide segments and thus increased chain rigidity. Furthermore, the bulky substituents in the main chain generally tend to increase FFV and hence gas permeability [26]. Kwon et al. reported a series of PIs from commercial diamines, 2,2′-bis(4′′-tert-butylphenyl)-4,4′,5,5′-biphenyltetracarboxylicdianhydride and 2,2′-bis(4′′-trimethylsilylphenyl)-4,4′,5,5′-biphenyltetracarboxylic dianhydride [27]. The gas permeability in these PIs was significantly enhanced by the introduction of bulky 4′′-tert-butylphenyl or 4′′-trimethylsilylphenyl substituents, with their O2 permeability and O2/N2 selectivity being 31–110 Barrer and 2.8–4.3, respectively. Zhang et al. reported PIs from 2,2′-phenoxyl-substituted BPDA [26]. The results indicated that O2 permeability increased with the size of the substituents, following the order of tert-butyl phenoxyl > methyl phenoxyl > phenoxyl, while their O2/N2 selectivity followed the opposite trend, ranging from 3.8 to 4.6. Bromine has a larger Van der Waals volume (Vw) of 14.60 cm3 mol−1 than many other groups, such as -Cl (12.00 cm3 mol−1), -CH3 (13.67 cm3 mol−1), -NH2 (7.44 cm3 mol−1) and -OH (8.00 cm3 mol−1). Recently, Zhao and co-workers synthesized PIM-PIs derived from dibromo substituted fluorine-containing diamines [28]. The results showed that introducing bromine substituents can considerably improve the ability to resist physical aging. Furthermore, the high Vw value of the bromo group is conducive to improving gas permeability [29].
Hence, in this work, we reported PIM-PIs from 2,2′-dibromo- 4,4′,5,5′-bipohenyltetracarboxylic dianhydride (Br-BPDA) and five typical twisted diamines, i.e., (7,7′-(mesitylmethylene)bis(8-methyldibenzo[b,e][1,4]dioxin-2-amine) (MMBMA), 7,7′-(Mesitylmethylene)bis(1,8-dimethyldibenzo[b,e][1,4] dioxin-2-amine) (MMBDA), 4,10-dimethyl-6H,12H-5,11-methanodibenzo[b,f][1,5]diazocine-2,8-diamine (TBDA1), 4,10-dimethyl-6H,12H-5,11-methanodibenzo[b,f][1,5]diazocine-3,9-diamine (TBDA2), and (9R,10R)-9,10-dihydro-9,10-[1,2]benzenoanthracene-2,6-diamine (DAT). A systematic study was conducted on the physical properties, microporous characteristics, and FFV of these polymers, and their performances regarding gas separation were evaluated.

2. Materials and Methods

2.1. Materials

4,4′-BPDA was obtained from China Tech Chemical Co., Ltd. (Tianjin, China), and dried at 250 °C under vacuum prior to use. N-Methylpyrrolidone (NMP), m-cresol, and ethanol were purchased from Energy Chemical Co., Ltd. (Shanghai, China). m-cresol and NMP were distilled over calcium hydride and stored in argon-purged bottles. All other chemicals were obtained from J&K Scientific Ltd. (Beijing, China) and were used as received. The synthesis methods of Br-BPDA [30], MMBMA, MMBDA [31], TBDA1, TBDA2 [12], and DAT [32] came from publications.

2.2. Polymer Synthesis

The Br-BPDA-derived polyimides were synthetized by a one-step solution polycondensation method in m-cresol.
Br-BPDA-DAT: Br-BPDA (0.9002 g, 2.00 mmol), DAT (0.5688 g, 2.00 mmol), benzoic acid (0.5446 g, 4.00 mmol), and m-cresol (3.4 mL) were added in a 20 mL flask with three-necked under nitrogen at 90 °C. Once the mixture became homogeneous, the reaction temperature was raised to 190 °C and held for 6 h. After cooling to 100 °C, the resulting viscous solutions were poured slowly into a mixture of methanol (50.0 mL) and deionized water (50.0 mL). The fibrous polymers were collected and purified by re-dissolution in chloroform and precipitation into methanol thrice. In a Soxhlet extractor, the PIs were then purified with methanol for 48 h and dried under vacuum at 140 °C for 8 h to obtain Br-BPDA-DAT (0.6978 g, yield: 95%). 1H NMR (400 MHz, DMSO-d6): δ 8.40 (s, 2H), 7.94 (s, 2H), 7.63–7.52 (m, 6H), 7.14–7.05 (m, 4H), 5.84 (s, 2H). FT-IR: 2969, 2917, 2858 cm−1 (C-H), 1781 cm−1 (C=O), 1728 cm−1 (C=O), 1376 cm−1 (C-N-C), 598 cm−1 (C-Br).
Br-BPDA-MMBDA: This polymer was prepared according to a procedure similar to Br-BPDA-DAT, yield: 88%. 1H NMR (400 MHz, CDCl3): δ 8.27 (s, 2H), 7.78 (s, 2H), 6.82–6.74 (m, 8H), 6.35 (s, 2H), 5.46 (s, 1H), 2.26–1.68 (m, 21H). FT-IR: 2969, 2917, 2858 cm−1 (C-H), 1781 cm−1 (C=O), 1728 cm−1 (C=O), 1376 cm−1 (C-N-C), 598 cm−1 (C-Br).
Br-BPDA-MMBMA: This polymer was prepared according to a procedure similar to Br-BPDA-DAT, yield: 93%. 1H NMR (400 MHz, CDCl3): δ 8.30 (s, 2H), 7.80 (s, 2H), 6.95–6.68 (m, 10H), 6.34 (s, 2H), 5.45 (s, 1H), 2.25–1.98 (m, 15H). FT-IR: 2969, 2917, 2858 cm−1 (C-H), 1780 cm−1 (C=O), 1728 cm−1 (C=O), 1376 cm−1 (C-N-C), 598 cm−1 (C-Br).
Br-BPDA-TBDA1: This polymer was prepared according to a procedure similar to Br-BPDA-DAT, yield: 89%. 1H NMR (400 MHz, CDCl3): δ 8.26 (s, 2H), 7.78 (s, 2H), 7.11 (s, 2H), 6.86 (s, 2H), 4.66 (d, 2H), 4.33 (s, 2H), 4.08 (d, 2H), 2.45 (s, 6H). FT-IR: 2969, 2917, 2858 cm−1 (C-H), 1781 cm−1 (C=O), 1728 cm−1 (C=O), 1376 cm−1 (C-N-C), 599 cm−1 (C-Br).
Br-BPDA-TBDA2: This polymer was prepared according to a procedure similar to Br-BPDA-DAT, yield: 92%. 1H NMR (400 MHz, CDCl3): δ 8.35 (d, 2H), 7.87 (d, 2H), 7.00 (s, 4H), 4.70 (d, 2H), 4.38 (s, 2H), 4.12 (d, 2H), 2.30 (d, 6H). FT-IR: 2969, 2917, 2858 cm−1 (C-H), 1780 cm−1 (C=O), 1728 cm−1 (C=O), 1376 cm−1 (C-N-C), 599 cm−1 (C-Br).

2.3. Membrane Casting

The chloroform solutions (3 wt%) of the Br-BPDA-derived polymers were purified through 1 μm PTFE filters and cast onto glass panels. They were dried at room temperature for three days to remove chloroform. Specially, Br-BPDA-DAT was dissolved in NMP (3 wt%), and the solvent was depleted by drying at 60 °C for 5 h, 150 °C for 1 h, 200 °C for 1 h, and 250 °C for 4 h in vacuum.

2.4. Characterization

Fourier-transform infrared (FT-IR) spectra and 1H NMR spectra were obtained on a Cary660+620 Micro FTIR instrument (Agilent, Santa Clara, CA, USA) and Bruker Advance Neo 600 spectrometer (Bruker, Rheinstetten, Germany), respectively. Number average molecular weights (Mn), weight average molecular weights (Mw), and polydispersity indices (PDI) were measured on TOSOH HLC-8420GPC (TOSOH, Tokyo, Japan) gel permeation chromatography (GPC) equipped with a refractive index detector using dimethylformamide (DMF + LiBr 0.1 wt%) as the eluent at a flow rate of 0.3 mL min−1 and polystyrene as the calibration standard at 40 °C. Wide-angle X-ray diffraction (WAXD) was performed on a Bruker D8 Advance Davinci instrument (Bruker, Karlsruhe, Germany) with Cu Kα radiation (λ = 1.54 Å) and an angular range from 5° to 50°. The storage modulus and tan δ of the Br-BPDA-derived PIM-PIs were studied using a Q850 DMA (TA Instruments, New Castle, DE, USA) at a heating rate of 5 °C min−1. Thermogravimetric analysis (TGA) was performed on a Q55 TGA (TA Instruments, New Castle, DE, USA) at a heating rate of 10 °C min−1 in nitrogen. Brunauer–Emmett–Teller surface areas (SBET) were measured via N2 adsorption at 77 K using an ASAP 2460 instrument (Micromeritics Instrument Corporation, Norcross, GA, USA). Tensile testing was performed on a TCS-2000 electron tensile testing machine (Gotech Testing Machines Inc., Taichung City, Taiwan) at a constant displacement rate of 2 mm min−1. Contact angles were obtained using a sessile drop water with a Dataphysics OCA-20 contact angle analyzer. The density of the Br-BPDA-derived PIM-PIs were obtained using an SQP balance (Sartorius, Gottingen, Germany) equipped with a density measurement kit. The FFV of the Br-BPDA-derived PIM-PIs was calculated using the group contribution method in the literature [10,33]. The gas permeabilities of the Br-BPDA-derived PIM-PIs were measured on a PERME VAC-2 permeation system (Labthink Instruments Co., Ltd., Jinan, China) at 1 bar and 35 °C [34].

3. Results and Discussion

3.1. Synthesis of Polymers

According to previous reports, polyimides derived from 2,2′-disubstituted BPDA exhibit better solubility than those based on 4,4′-BPDA [24,25]. And, given the close Vw values of Br-BPDA and 6FDA (161.12 vs. 184.75 cm3 mol−1) [35], it could be anticipated that that polyimides from Br-BPDA have a similar FFV to those based on 6FDA. Meanwhile, MMBMA, MMBDA, TBDA1, TBDA2, and DAT have been extensively used for the preparation of PIM-PIs with a high FFV [12,31,32]. In this work, PIM-PIs were obtained by combining Br-BPDA with five typical rigid and twisted diamines through high-temperature solution polymerization (Scheme 1). The Mw and PDI values of these polymers were 18.0–45.0 kg mol−1 and 1.8–3.8 (Table 1), respectively. Br-BPDA-MMBMA exhibited the highest molecular weight, which may be attributed to the high reactivity of MMBMA. The FT-IR spectra of the Br-BPDA-derived polymers are shown in Figure S1, and the successful synthesis of the imine ring structure are demonstrated by the characteristic peaks at ~1770 cm−1 (asymmetric C=O stretching), ~1730 cm−1 (symmetric C=O stretching), and ~1360 cm−1 (C-N stretching). Moreover, the absorption peaks of amide or amino groups, located at ~3350 cm−1 (asymmetric N-H stretching vibration), ~3170 cm−1 (symmetric N-H stretching), ~1650 cm−1 (N-H bending) completely disappear, indicating the complete reaction of diamine with no residual diamine molecules in the polymer chain. And, in the 1H NMR spectra (Figure S2), the peaks at 8.3 ppm and 7.8 ppm represent the aromatic ring protons in the Br-BPDA residues. The absence of peaks for -NH2 and -COOH groups also proves the successful preparation of polyimides. Additionally, the chemical structure of Br-BPDA-DAT is further confirmed by 13C NMR (Figure S4), where the features are fully assigned. These results confirm the successful synthesis of Br-BPDA-derived PIM-PIs.
All the Br-BPDA-derived PIs exhibited good solubility in high-boiling-point solvents due to the introduction of bromine substituents (Table S1). In addition, the PIs with TB and dibenzodioxane segments were soluble in low-boiling-point solvents like CHCl3. In contrast, Br-BPDA-DAT exhibited relatively poor solubility in the overall series perhaps due to the unique Trip structure in DAT leading to a higher aromatic ring content. Due to the lower chain packing density (Table 2), Br-BPDA-MMBDA and Br-BPDA-MMBMA showed the best solubility. These polymers showed high modulus (59.2–109.3 MPa) and good strength (1.8–2.2 GPa), indicating that they have outstanding mechanical properties (Table 1 and Figure S4). The glass transition temperatures (Tg) of these polymers were obtained by DMA testing (Figure 1), and all Tg values were higher than 400 °C. In particular, the Tg of Br-BPDA-DAT was higher than 500 °C. The Tg values of these PIM-PIs followed the order of Br-BPDA-MMBMA < Br-BPDA-TBDA1 < Br-BPDA-TBDA2 < Br-BPDA-MMBDA < Br-BPDA-DAT. Br-BPDA-MMBMA exhibited the lowest Tg due to its relatively low chain rigidity, resulting from the absence of ortho-positioned methyl substituents.
The contact angles of the Br-BPDA-derived PIM-PIs were 95.0–103.9° (Figure S5). The hydrophobicity of these polymers can be explained by their relatively lower imide contents, as well as the methyl substituents for some cases.

3.2. Microstructural Properties

It can be observed that there were significant hysteresis loops and a higher nitrogen absorption at a relatively low pressure in the nitrogen adsorption desorption isotherm, both of which were obvious characteristics of intrinsic microporous polymers (Figure 2a) [11]. The values of SBET ranged from 211 to 342 m2 g−1, with the order of Br-BPDA-TBDA1 < Br-BPDA-DAT < Br-BPDA-TBDA2 < Br-BPDA-MMBMA < Br-BPDA-MMBDA. And, the value of SBET for Br-BPDA-MMBDA was 21% higher than that of Br-BPDA-MMBMA, and the value of SBET for Br-BPDA-TBDA2 was 64% higher than that of Br-BPDA-TBDA1, which is also consistent with the value of the FFV. It can be deduced that the introduction of bulky bromine atoms and ortho-positioned methyl group will restrain the chain densification of PI, open the polymer backbone, and induce a larger free volume [23].
The CO2 uptake is affected by the CO2 affinity and specific surface areas of polymers [2]. For these Br-BPDA-derived PIM-PIs, at 273 K and P/P0 = 0.029, the CO2 uptake ranged from 26.1 to 30.4 cm3 g−1 (Figure 2b and Table 2). Among them, Br-BPDA-TBDA1/TBDA2 exhibited a higher CO2 uptake because of the dipole–quadrupole interaction between the tertiary amine in the TB skeleton and the polarized CO2 molecule [12,36,37,38]. This result also demonstrates that ortho-positioned methyl groups have a similar effect on the surface areas of polymers, like Br-BPDA-TBDA1(29.3 cm3 g−1) < Br-BPDA-TBDA2 (30.4 cm3 g−1) and Br-BPDA-MMBMA (26.1 cm3 g−1) < Br-BPDA-MMBDA (28.1 cm3 g−1). This indicates that ortho-substituted groups (-Br and -CH3) hinder rotational chemical bonds and have an impact on the surface, which is consistent with the FFV and SBET results.
The cumulative volume of micropores (VM) for these polymers spanned a range of 0.030–0.045 cm3 g−1. Br-BPDA-MMBDA/MMBMA showed a relatively lower VM value, owing to the relatively low rigidity of dibenzodioxane moieties relative to TB or Trip segments. In addition, the VM values of Br-BPDA-TBDA1 were lower than Br-BPDA-TBDA2, and the VM values of Br-BPDA-MMBMA were lower than Br-BPDA-MMBDA, respectively, due to the absence of an ortho substituents methyl group.
Regarding density, according to Bondi’s group contribution method [35,39], the values of the FFV of these polyimides, ranged from 0.169 to 0.216 (Table 2). And, similar tendencies were observed for the FFV and SBET of these polymers. The chain packing profiles of the Br-BPDA-derived PIM-PIs were characterized by WAXD measurements (Figure 3 and Table 2). The diffraction peaks were mainly located in the range of 10–30°, indicating their amorphous features. The average distances between different molecular chains of the corresponding PIM-PIs were in the range of 4.92–5.88 and 3.75–3.94 Å, respectively. Two major peaks were fitted in these diffraction peaks (labelled as dA and dB) [40,41], where dA and dB were respectively assigned to the interchain distances and the π-π stacking interactions. The effect of ortho substituents on d-spacing was also observed in WAXD curves, the dA value of Br-BPDA-MMBMA < Br-BPDA-MMBDA, and the dA value of Br-BPDA-TBDA1 < Br-BPDA-TBDA2. Additionally, a shoulder peak was also observed at around 10°, which corresponded to the larger micropores in the PIM-PIs. The result is beneficial for improving gas permeability. The amorphous feature was a typical characteristic of the PIM-PI that could be applied to gas separation. This tendency was consistent with the FFV and SBET of the polymers.

3.3. Gas Separation Performance

The water and CO2 in the air can cause the film to plasticize, increasing the FFV and reducing the gas selectivity of the polymers [42]. So, before conducting gas separation tests, it was necessary to soak the fresh membranes in methanol for one day, which was beneficial for improving the gas separation performance [43], and then dry them under vacuum at 100 °C to remove methanol and H2O from the membranes. The pure gas transport properties of these PIs were investigated with gases including H2, CO2, O2, N2, and CH4. Their gas permeabilities and selectivities are shown in Table 3. For the given polymers, the gas permeabilities of these polymers were in the order of PCO2 > PH2 > PO2 > PCH4 > PN2. However, after ageing for 300 or 900 days, the order between PCH4 and PN2 was reversed. For instance, the PH2, PCO2, PO2, PN2, and PCH4 of Br-BPDA-MMBDA (FFV = 0.216) were 576.5, 724.5, 143.2, 42.9, and 61.7 Barrer, respectively, which were 1.6–3.1 times greater than those of Br-BPDA-DAT (FFV = 0.189). In addition, Br-BPDA-TBDA1 (FFV = 0.169), Br-BPDA-TBDA2 (FFV = 0.177), and Br-BPDA-DAT (FFV = 0.189) showed moderate gas permeabilities despite their smaller FFV because of the Trip and TB groups, leading to higher rigidity. However, compared with Br-BPDA-TBDA1, Br-BPDA-TBDA2 was more permeable due to the presence of ortho-substituted methyl groups, leading to insufficient space for the free rotation of C-N bonds in the imide rings. Br-BPDA-MMBDA exhibited the lowest selectivity due to its moderate FFV but a low cumulative micropore volume (Figure 2c). In contrary, Br-BPDA-TBDA1 displayed the highest selectivity because of the lowest d-spacing (dA = 4.92 Å) and FFV. In these PIs containing TB or Trip structures, the unique rigid structure gave the polymer a higher cumulative volume of ultramicropores, while strong π-π stacking interactions gave the polymer a higher gas sieving ability [44]. The synergistic effect of these two factors maintained a good balance between permeability and selectivity.
The gas separation performance of the Br-BPDA-derived PIM-PIs with other commercial membranes was also compared according to Robeson’s upper bounds (Figure 4). The Br-BPDA-derived PIM-PIs exhibited better performances than most commercial polymers, such as Matrimid® 5218, P84® [3,44,45,46,47,48,49,50,51,52,53]. However, the Br-BPDA-derived polymers showed a slightly inferior or similar performance regarding gas separation compared to their counterparts based on 6FDA due to the slightly lower Vw of Br-BPDA than 6FDA (161.12 vs. 184.75 cm3 mol−1) [12,39,42,45].
The physical aging characteristics of the Br-BPDA-derived PIM-PIs were systematically assessed. The gas separation performances of fresh membranes and those aged membranes were shown in Figure 4 and Table 3. The permeabilities of all the PIM-PIs decreased, and the selectivities increased due to the collapse of larger micropores and the decrease in FFV. The loss in gas permeability was most pronounced in gases with larger kinetic diameters, resulting in the improved selectivity of H2/N2, H2/CH4, and CO2/CH4. Zhao et al. [28,29] investigated the effect of -Br groups on the physical aging of polymer membranes and found that the bromo groups could effectively retard the speed of physical aging by the interference with the nearby carbonyl groups and restricted rotation. Similar trends were also observed in this work. The H2 permeability of all the Br-BPDA-derived PIM-PIs decreased by only 26.7–41.5% after aging for 300 days and 45.2–68.6% for 900 days (Figure 5). In addition, the gas separation performance of all the aged membranes was well retained or even improved compared to the fresh membranes, indicating their excellent resistance to physical ageing.

4. Conclusions

Five high-molecular weight PIM-PIs were prepared from Br-BPDA and different diamines (MMBMA, MMBDA, TBDA1, TBDA2, and DAT) via the “one-step” method in m-cresol. These Br-BPDA-derived PIM-PIs exhibited extremely high Tg (>400 °C) because of their twisted structure from diamines and ortho-substituted groups (-Br and -CH3) hinder rotational chemical bonds. And, the Br-BPDA-derived PIM-PIs showed favorable mechanical properties for gas separation application, tensile strength > 59.2 MPa, modulus > 1.8 GPa, and elongation at break > 3.4%. The markedly high d-spacing values of the polymers (>0.492 nm) were observed due to the incorporation of large bromine substituents and a twisted diamine monomer. Br-BPDA-MMBDA displayed the highest gas permeability but lowest perm-selectivity due to its highest FFV (0.216) and lowest cumulative volume of micropores, leading to its relatively poor gas separation performance. On the contrary, Br-BPDA-DAT showed high perm-selectivity while maintaining moderate gas permeability due to the high rigidity and unique internal FFV of Trip moieties. Moreover, the gas separation performance of Br-BPDA-derived PIM-PIs improved with the ageing time, indicative their excellent resistance to physical ageing due to the relatively high chain rigidity resulting from the presence of ortho-substituted -Br and -CH3 groups. This work provides a new insight into advancing the design of PIM-PIs with long-term stability for gas separations.

Supplementary Materials

The following supporting information can be downloaded at: https://www.mdpi.com/article/10.3390/polym16091198/s1, Figure S1: FT-IR spectra of Br-BPDA-derived PIM-PIs; Figure S2: 1H NMR spectra of Br-BPDA-derived PIM-PIs; Figure S3: 13C NMR spectrum of Br-BPDA-DAT in DMSO-d6; Figure S4: Stress–strain curves of Br-BPDA-derived PIM-PIs; Figure S5: Data of water contact angle on the Br-BPDA-derived PIM-PIs surface. Table S1: Solubility of Br-BPDA-derived PIM-PIs; Table S2: List of abbreviations, acronyms, and symbols.

Author Contributions

Conceptualization, Y.L. (Yongle Li) and Y.L. (Yao Lu); methodology, Y.L. (Yongle Li) and Y.L. (Yao Lu); formal analysis, Y.L. (Yongle Li) and C.T.; investigation, Y.L. (Yongle Li) and C.T.; resources, Z.W. and J.Y.; writing—original draft preparation, Y.L. (Yongle Li) and C.T.; writing—review and editing, C.T. and J.Y.; visualization, Y.L. (Yongle Li) and C.T.; supervision, Z.W. and J.Y.; project administration, Z.W. and J.Y.; funding acquisition, Z.W. and J.Y. All authors have read and agreed to the published version of the manuscript.

Funding

This research was funded by the National Key R&D Program of China (2023YFB3709700), the Leading Innovative and Entrepreneur Team Introduction Program of Zhejiang (No. 2021R01005), and the Key Technical Development Program of Ningbo (2021Z091), whom we thank for the financial support.

Institutional Review Board Statement

Not applicable.

Data Availability Statement

Data are contained within the article.

Conflicts of Interest

The authors declare no conflicts of interest.

References

  1. Hosseini, S.S.; Chung, T.S. Carbon membranes from blends of PBI and polyimides for N2/CH4 and CO2/CH4 separation and hydrogen purification. J. Membr. Sci. 2009, 328, 174–185. [Google Scholar] [CrossRef]
  2. Lu, Y.; Hu, X.; Pang, Y.; Miao, J.; Zhao, J.; Nie, W.; Wang, Z.; Yan, J. Intrinsically microporous polyimides derived from norbornane-2-spiro-α-cyclopentanone-α′-spiro-2″-norbornane-5,5″,6,6″-tetracarboxylic dianhydride. Polymer 2021, 228, 123955. [Google Scholar] [CrossRef]
  3. Koros, W.J.; Fleming, G.K.; Jordan, S.M.; Kim, T.H.; Hoehn, H.H. Polymeric membrane materials for solution-diffusion based permeation separations. Prog. Polym. Sci. 1988, 13, 339–401. [Google Scholar] [CrossRef]
  4. Robeson, L.M. The upper bound revisited. J. Membr. Sci. 2008, 320, 390–400. [Google Scholar] [CrossRef]
  5. Carta, M.; Malpass-Evans, R.; Croad, M.; Rogan, Y.; Jansen, J.C.; Bernardo, P.; Bazzarelli, F.; McKeown, N.B. An efficient polymer molecular sieve for membrane gas separations. Science 2013, 339, 303–307. [Google Scholar] [CrossRef] [PubMed]
  6. Guiver, M.D.; Lee, Y.M. Materials science. Polymer rigidity improves microporous membranes. Science 2013, 339, 284–285. [Google Scholar] [CrossRef]
  7. Park, H.B.; Jung, C.H.; Lee, Y.M.; Hill, A.J.; Pas, S.J.; Mudie, S.T.; Van Wagner, E.; Freeman, B.D.; Cookson, D.J. Polymers with cavities tuned for fast selective transport of small molecules and ions. Science 2007, 318, 254–258. [Google Scholar] [CrossRef]
  8. Low, Z.X.; Budd, P.M.; McKeown, N.B.; Patterson, D.A. Gas permeation properties, physical aging, and its mitigation in high free volume glassy polymers. Chem. Rev. 2018, 118, 5871–5911. [Google Scholar] [CrossRef] [PubMed]
  9. Swaidan, R.; Ghanem, B.; Litwiller, E.; Pinnau, I. Physical aging, plasticization and their effects on gas permeation in “rigid” polymers of intrinsic microporosity. Macromolecules 2015, 48, 6553–6561. [Google Scholar] [CrossRef]
  10. Hu, X.; Lee, W.H.; Bae, J.Y.; Zhao, J.; Kim, J.S.; Wang, Z.; Yan, J.; Lee, Y.M. Highly permeable polyimides incorporating Tröger’s base (TB) units for gas separation membranes. J. Membr. Sci. 2020, 615, 118533. [Google Scholar] [CrossRef]
  11. Ghanem, B.S.; McKeown, N.B.; Budd, P.M.; Selbie, J.D.; Fritsch, D. High-performance membranes from polyimides with intrinsic microporosity. Adv. Mater. 2008, 20, 2766–2771. [Google Scholar] [CrossRef] [PubMed]
  12. Wang, Z.; Wang, D.; Zhang, F.; Jin, J. Troger’s base-based microporous polyimide membranes for high-performance gas separation. ACS Macro Lett. 2014, 3, 597–601. [Google Scholar] [CrossRef] [PubMed]
  13. Tsui, N.T.; Paraskos, A.J.; Torun, L.; Swager, T.M.; Thomas, E.L. Minimization of internal molecular free volume:  A mechanism for the simultaneous enhancement of polymer stiffness, strength, and ductility. Macromolecules 2006, 39, 3350–3358. [Google Scholar] [CrossRef]
  14. Swaidan, R.; Ghanem, B.; Pinnau, I. Fine-tuned intrinsically ultramicroporous polymers redefine the permeability/selectivity upper bounds of membrane-based air and hydrogen separations. ACS Macro Lett. 2015, 4, 947–951. [Google Scholar] [CrossRef]
  15. Comesaña-Gándara, B.; Chen, J.; Bezzu, C.G.; Carta, M.; Rose, I.; Ferrari, M.-C.; Esposito, E.; Fuoco, A.; Jansen, J.C.; McKeown, N.B. Redefining the Robeson upper bounds for CO2/CH4 and CO2/N2 separations using a series of ultrapermeable benzotriptycene-based polymers of intrinsic microporosity. Energy Environ. Sci. 2019, 12, 2733–2740. [Google Scholar] [CrossRef]
  16. Liaw, D.J.; Wang, K.L.; Huang, Y.C.; Lee, K.R.; Lai, J.Y.; Ha, C.S. Advanced polyimide materials: Syntheses, physical properties and applications. Prog. Polym. Sci. 2012, 37, 907–974. [Google Scholar] [CrossRef]
  17. McKeown, N.B. The synthesis of polymers of intrinsic microporosity (PIMs). Sci. China Chem. 2017, 60, 1023–1032. [Google Scholar] [CrossRef]
  18. Ghanem, B.S.; McKeown, N.B.; Budd, P.M.; Al-Harbi, N.M.; Fritsch, D.; Heinrich, K.; Starannikova, L.; Tokarev, A.; Yampolskii, Y. Synthesis, characterization, and gas permeation properties of a novel group of polymers with intrinsic microporosity: PIM-polyimides. Macromolecules 2009, 42, 7881–7888. [Google Scholar] [CrossRef]
  19. Marjani, A.; Nakhjiri, A.T.; Taleghani, A.S.; Shirazian, S. Mass transfer modeling absorption using nanofluids in porous polymeric membranes. J. Mol. Liq. 2020, 318, 114115. [Google Scholar] [CrossRef]
  20. Rostami, A.; Baghban, A.; Shirazian, S. On the evaluation of density of ionic liquids: Towards a comparative study. Chem. Eng. Res. Des. 2019, 147, 648–663. [Google Scholar] [CrossRef]
  21. Friess, K.; Izak, P.; Karaszova, M.; Pasichnyk, M.; Lanc, M.; Nikolaeva, D.; Luis, P.; Jansen, J.C. A review on ionic liquid gas separation membranes. Membranes 2021, 11, 97. [Google Scholar] [CrossRef] [PubMed]
  22. Lu, Y.; Hu, X.; Lee, W.H.; Bae, J.Y.; Zhao, J.; Nie, W.; Wang, Z.; Yan, J.; Lee, Y.M. Effects of bulky 2,2′-substituents in dianhydrides on the microstructures and gas transport properties of thermally rearranged polybenzoxazoles. J. Membr. Sci. 2021, 639, 119777. [Google Scholar] [CrossRef]
  23. Tanaka, K.; Kita, H.; Okamoto, K.; Nakamura, A.; Kusuki, Y. Gas permeability and permselectivity in polyimides based on 3,3’,4,4’-biphenyltetracarboxylic dianhydride. J. Membr. Sci. 1989, 47, 203–215. [Google Scholar] [CrossRef]
  24. Li, F.; Ge, J.J.; Honigfort, P.S.; Fang, S.; Chen, J.-C.; Harris, F.W.; Cheng, S.Z.D. Dianhydride architectural effects on the relaxation behaviors and thermal and optical properties of organo-soluble aromatic polyimide films. Polymer 1999, 40, 4987–5002. [Google Scholar] [CrossRef]
  25. Li, F.; Fang, S.; Ge, J.J.; Honigfort, P.S.; Chen, J.C.; Harris, F.W.; Cheng, S.Z.D. Diamine architecture effects on glass transitions, relaxation processes and other material properties in organo-soluble aromatic polyimide films. Polymer 1999, 40, 4571–4583. [Google Scholar] [CrossRef]
  26. Qiu, Z.; Chen, G.; Zhang, Q.; Zhang, S. Synthesis and gas transport property of polyimide from 2,2′-disubstituted biphenyltetracarboxylic dianhydrides (BPDA). Eur. Polym. J. 2007, 43, 194–204. [Google Scholar] [CrossRef]
  27. Kim, H.-S.; Kim, Y.-H.; Ahn, S.-K.; Kwon, S.-K. Synthesis and characterization of highly soluble and oxygen permeable new polyimides bearing a noncoplanar twisted biphenyl unit containing tert-butylphenyl or trimethylsilyl phenyl groups. Macromolecules 2003, 36, 2327–2332. [Google Scholar] [CrossRef]
  28. Zhao, W.; Zhang, J.; Liu, C.; Ma, Y.; Li, K.; Guo, M.; Jiao, L.; Ma, X.; Yang, L.; Yang, S.; et al. Fine-tuning gas separation performance of intrinsic microporous polyimide by the regulation of atomic-level halogen substitution. J. Membr. Sci. 2024, 692, 122317. [Google Scholar] [CrossRef]
  29. Zhao, W.; Li, K.; Ma, Y.; Gao, Y.; Zhang, J.; Zhou, L.; Wang, W.; Wang, J.; Ma, Y.; Guo, M.; et al. Simultaneously enhanced gas separation and anti-aging performance of intrinsic microporous polyimide by dibromo substitution. J. Membr. Sci. 2023, 687, 122081. [Google Scholar] [CrossRef]
  30. Harris, F.W.; Lin, S.-H.; Li, F.; Cheng, S.Z.D. Organo-soluble polyimides: Synthesis and polymerization of 2,2′-disubstituted-4,4′,5,5′-biphenyltetracarboxylic dianhydrides. Polymer 1996, 37, 5049–5057. [Google Scholar] [CrossRef]
  31. Hu, X.; Pang, Y.; Mu, H.; Meng, X.; Wang, X.; Wang, Z.; Yan, J. Synthesis and gas separation performances of intrinsically microporous polyimides based on 4-methylcatechol-derived monomers. J. Membr. Sci. 2021, 620, 118825. [Google Scholar] [CrossRef]
  32. Zhang, C.; Fu, L.; Tian, Z.; Cao, B.; Li, P. Post-crosslinking of triptycene-based Tröger’s base polymers with enhanced natural gas separation performance. J. Membr. Sci. 2018, 556, 277–284. [Google Scholar] [CrossRef]
  33. Hu, X.; Lee, W.H.; Zhao, J.; Kim, J.S.; Wang, Z.; Yan, J.; Zhuang, Y.; Lee, Y.M. Thermally rearranged polymer membranes containing highly rigid biphenyl ortho-hydroxyl diamine for hydrogen separation. J. Membr. Sci. 2020, 604, 118053. [Google Scholar] [CrossRef]
  34. Hu, X.; Lee, W.H.; Bae, J.Y.; Kim, J.S.; Jung, J.T.; Wang, H.H.; Park, H.J.; Lee, Y.M. Thermally rearranged polybenzoxazole copolymers incorporating Tröger’s base for high flux gas separation membranes. J. Membr. Sci. 2020, 612, 118437. [Google Scholar] [CrossRef]
  35. Bondi, A. Van der Waals Volumes and Radii. J. Phys. Chem. 2002, 68, 441–451. [Google Scholar] [CrossRef]
  36. Jung, C.H.; Lee, Y.M. Gas permeation properties of hydroxyl-group containing polyimide membranes. Macromol. Res. 2008, 16, 555–560. [Google Scholar] [CrossRef]
  37. Hao, G.P.; Li, W.C.; Qian, D.; Lu, A.H. Rapid synthesis of nitrogen-doped porous carbon monolith for CO2 capture. Adv. Mater. 2010, 22, 853–857. [Google Scholar] [CrossRef] [PubMed]
  38. Hu, X.; Lee, W.H.; Zhao, J.; Bae, J.Y.; Kim, J.S.; Wang, Z.; Yan, J.; Zhuang, Y.; Lee, Y.M. Tröger’s Base (TB)-containing polyimide membranes derived from bio-based dianhydrides for gas separations. J. Membr. Sci. 2020, 610, 118255. [Google Scholar] [CrossRef]
  39. Lee, W.M. Selection of barrier materials from molecular structure. Polym. Eng. Sci. 2004, 20, 65–69. [Google Scholar] [CrossRef]
  40. Turner-Jones, A. Development of the γ-crystal form in random copolymers of propylene and their analysis by dsc and X-ray methods. Polymer 1971, 12, 487–508. [Google Scholar] [CrossRef]
  41. Huo, H.; Jiang, S.; An, L.; Feng, J. Influence of shear on crystallization behavior of the β phase in isotactic polypropylene with β-nucleating agent. Macromolecules 2004, 37, 2478–2483. [Google Scholar] [CrossRef]
  42. Rodriguez, M.K.; Lin, S.; Wu, A.X.; Storme, K.R.; Joo, T.; Grosz, A.F.; Roy, N.; Syar, D.; Benedetti, F.M.; Smith, Z.P. Penetrant-induced plasticization in microporous polymer membranes. Chem. Soc. Rev. 2024, 53, 2435–2529. [Google Scholar] [CrossRef]
  43. Seong, J.G.; Zhuang, Y.; Kim, S.; Do, Y.S.; Lee, W.H.; Guiver, M.D.; Lee, Y.M. Effect of methanol treatment on gas sorption and transport behavior of intrinsically microporous polyimide membranes incorporating Tröger’s base. J. Membr.Sci. 2015, 480, 104–114. [Google Scholar] [CrossRef]
  44. Kim, S.; Lee, Y.M. Rigid and microporous polymers for gas separation membranes. Prog. Polym. Sci. 2015, 43, 1–32. [Google Scholar] [CrossRef]
  45. Li, J.; Wang, S.; Nagai, K.; Nakagawa, T.; Mau, A.W.H. Effect of polyethyleneglycol (PEG) on gas permeabilities and permselectivities in its cellulose acetate (CA) blend membranes. J. Membr. Sci. 1998, 138, 143–152. [Google Scholar] [CrossRef]
  46. Huang, Z.; Li, Y.; Wen, R.; May Teoh, M.; Kulprathipanja, S. Enhanced gas separation properties by using nanostructured PES-Zeolite 4A mixed matrix membranes. J. Appl. Polym. Sci. 2006, 101, 3800–3805. [Google Scholar] [CrossRef]
  47. Alghunaimi, F.; Ghanem, B.; Alaslai, N.; Swaidan, R.; Litwiller, E.; Pinnau, I. Gas permeation and physical aging properties of iptycene diamine-based microporous polyimides. J. Membr. Sci. 2015, 490, 321–327. [Google Scholar] [CrossRef]
  48. Muruganandam, N.; Koros, W.J.; Paul, D.R. Gas sorption and transport in substituted polycarbonates. J. Polym. Sci. B Polym. Phys. 1987, 25, 1999–2026. [Google Scholar] [CrossRef]
  49. Sridhar, S.; Veerapur, R.S.; Patil, M.B.; Gudasi, K.B.; Aminabhavi, T.M. Matrimid polyimide membranes for the separation of carbon dioxide from methane. J. Appl. Polym. Sci. 2007, 106, 1585–1594. [Google Scholar] [CrossRef]
  50. Abdulhamid, M.A.; Lai, H.W.H.; Wang, Y.; Jin, Z.; Teo, Y.C.; Ma, X.; Pinnau, I.; Xia, Y. Microporous polyimides from ladder diamines synthesized by facile catalytic arene–norbornene annulation as high-performance membranes for gas separation. Chem. Mater. 2019, 31, 1767–1774. [Google Scholar] [CrossRef]
  51. Ahn, J.; Chung, W.-J.; Pinnau, I.; Guiver, M.D. Polysulfone/silica nanoparticle mixed-matrix membranes for gas separation. J. Membr. Sci. 2008, 314, 123–133. [Google Scholar] [CrossRef]
  52. Abdulhamid, M.A.; Ma, X.; Miao, X.; Pinnau, I. Synthesis and characterization of a microporous 6FDA-polyimide made from a novel carbocyclic pseudo Tröger’s base diamine: Effect of bicyclic bridge on gas transport properties. Polymer 2017, 130, 182–190. [Google Scholar] [CrossRef]
  53. Dose, M.E.; Chwatko, M.; Hubacek, I.; Lynd, N.A.; Paul, D.R.; Freeman, B.D. Thermally cross-linked diaminophenylindane (DAPI) containing polyimides for membrane based gas separations. Polymer 2019, 161, 16–26. [Google Scholar] [CrossRef]
Polymers 16 01198 sch001
Scheme 1. Synthesis of Br-BPDA-derived polymers.
Scheme 1. Synthesis of Br-BPDA-derived polymers.
Polymers 16 01198 sch001
Polymers 16 01198 g001
Figure 1. (a) DMA curves and (b) TGA curves of Br-BPDA-derived PIM-PIs.
Figure 1. (a) DMA curves and (b) TGA curves of Br-BPDA-derived PIM-PIs.
Polymers 16 01198 g001
Polymers 16 01198 g002
Figure 2. (a) N2 adsorption/desorption isotherms, (b) CO2 absorption, (c) differential pore volume, (d) cumulative pore volumes of Br-BPDA-derived PIM-PIs.
Figure 2. (a) N2 adsorption/desorption isotherms, (b) CO2 absorption, (c) differential pore volume, (d) cumulative pore volumes of Br-BPDA-derived PIM-PIs.
Polymers 16 01198 g002
Polymers 16 01198 g003
Figure 3. WAXD patterns of Br-BPDA-derived PIM-PIs (Black line: Experimental data; Red line: Linear fitting curve of experimental data; Red point: The highest peak at dA).
Figure 3. WAXD patterns of Br-BPDA-derived PIM-PIs (Black line: Experimental data; Red line: Linear fitting curve of experimental data; Red point: The highest peak at dA).
Polymers 16 01198 g003
Polymers 16 01198 g004
Figure 4. Robeson plots of (a) H2/N2, (b) H2/CH4, (c) O2/N4, and (d) CO2/CH4 for Br-BPDA-derived PIM-PIs.
Figure 4. Robeson plots of (a) H2/N2, (b) H2/CH4, (c) O2/N4, and (d) CO2/CH4 for Br-BPDA-derived PIM-PIs.
Polymers 16 01198 g004
Polymers 16 01198 g005
Figure 5. Effect of physical aging time on gas permeability of Br-BPDA-derived PIM-PIs, (a) H2, (b) O2, (c) CH4, (d) CO2.
Figure 5. Effect of physical aging time on gas permeability of Br-BPDA-derived PIM-PIs, (a) H2, (b) O2, (c) CH4, (d) CO2.
Polymers 16 01198 g005
Table 1. Physicochemical properties of Br-BPDA-derived PIM-PIs.
Table 1. Physicochemical properties of Br-BPDA-derived PIM-PIs.
PolymerTg
(°C)		Td5
(°C)		Mw
(kg mol−1)		PDITensile Strength
(MPa)		Modulus
(GPa)		Elongation at Break (%)
Br-BPDA-MMBMA41644381.01.959.2 ± 7.02.1 ± 0.13.4 ± 0.6
Br-BPDA-MMBDA43245442.01.963.1 ± 0.52.0 ± 0.13.7 ± 0.2
Br-BPDA-TBDA141941645.01.978.5 ± 3.62.2 ± 0.14.9 ± 0.1
Br-BPDA-TBDA242841731.01.875.8 ± 5.61.8 ± 0.17.4 ± 1.4
Br-BPDA-DAT>50053852.03.8109.3 ± 7.02.1 ± 0.112.3 ± 1.1
Table 2. The microstructure of Br-BPDA-derived PIM-PIs.
Table 2. The microstructure of Br-BPDA-derived PIM-PIs.
PolymerSBET
(m2 g−1)		CO2 Uptake
(cm3 g−1)		D 1
(nm)		VM 2
(cm3 g−1)		dA
(Å)		dB
(Å)		Vw 3
(cm3 mol−1)		ρ
(g cm−3)		FFV
Br-BPDA-MMBMA25526.10.56/0.75/0.820.0305.513.76456.571.3280.190
Br-BPDA-MMBDA34228.10.58/0.78/0.860.0375.883.94470.171.2830.216
Br-BPDA-TBDA121129.30.54/0.78/0.860.0434.923.75304.351.4630.169
Br-BPDA-TBDA223930.40.58/0.77/0.860.0455.693.92304.351.4480.177
Br-BPDA-DAT23226.40.58/0.79/0.860.0395.233.76301.421.4490.189
1 Pore width. 2 Total volumes of micropores. 3 Van der Waals volume, calculated using the Bondi’s group contribution method [35].
Table 3. Gas separation performances of Br-BPDA-derived PIM-PIs.
Table 3. Gas separation performances of Br-BPDA-derived PIM-PIs.
Permeability (Barrer 1)Selectivity
PolymerH2CO2O2N2CH4H2/CH4H2/N2O2/N2CO2/N2CO2/CH4
Br-BPDA-MMBMA270.0315.555.114.119.014.219.13.9022.316.6
300 days aged198.0190.732.27.39.121.827.14.426.121.0
900 days aged147.9136.321.74.44.731.533.64.931.029.0
Br-BPDA-MMBDA576.5724.5143.242.961.79.413.43.316.911.8
300 days aged380.6476.981.320.127.313.918.94.023.717.5
900 days aged321.9399.062.315.119.016.921.34.126.421.0
Br-BPDA-TBDA1200.4161.627.76.27.327.632.54.526.222.2
300 days aged105.363.211.82.32.345.845.85.127.527.5
900 days aged73.236.96.71.21.073.261.05.630.836.9
Br-BPDA-TBDA2561.6711.0127.040.751.311.013.83.117.513.9
300 days aged370.9449.178.619.326.314.119.24.123.317.1
900 days aged240.5284.145.611.012.918.621.94.125.822.0
Br-BPDA-DAT349.8384.469.816.319.717.721.44.323.519.5
300 days aged204.3170.728.85.96.631.034.64.928.925.9
900 days aged109.889.015.32.82.740.739.25.531.833.0
1 1 Barrer = 10−10 [cm3 (STP) cm]/(cm2 s cm Hg).
Disclaimer/Publisher’s Note: The statements, opinions and data contained in all publications are solely those of the individual author(s) and contributor(s) and not of MDPI and/or the editor(s). MDPI and/or the editor(s) disclaim responsibility for any injury to people or property resulting from any ideas, methods, instructions or products referred to in the content.

Share and Cite

MDPI and ACS Style

Li, Y.; Lu, Y.; Tian, C.; Wang, Z.; Yan, J. Intrinsically Microporous Polyimides Derived from 2,2′-Dibromo-4,4′,5,5′-bipohenyltetracarboxylic Dianhydride for Gas Separation Membranes. Polymers 2024, 16, 1198. https://doi.org/10.3390/polym16091198

AMA Style

Li Y, Lu Y, Tian C, Wang Z, Yan J. Intrinsically Microporous Polyimides Derived from 2,2′-Dibromo-4,4′,5,5′-bipohenyltetracarboxylic Dianhydride for Gas Separation Membranes. Polymers. 2024; 16(9):1198. https://doi.org/10.3390/polym16091198

Chicago/Turabian Style

Li, Yongle, Yao Lu, Chun Tian, Zhen Wang, and Jingling Yan. 2024. "Intrinsically Microporous Polyimides Derived from 2,2′-Dibromo-4,4′,5,5′-bipohenyltetracarboxylic Dianhydride for Gas Separation Membranes" Polymers 16, no. 9: 1198. https://doi.org/10.3390/polym16091198

APA Style

Li, Y., Lu, Y., Tian, C., Wang, Z., & Yan, J. (2024). Intrinsically Microporous Polyimides Derived from 2,2′-Dibromo-4,4′,5,5′-bipohenyltetracarboxylic Dianhydride for Gas Separation Membranes. Polymers, 16(9), 1198. https://doi.org/10.3390/polym16091198

Note that from the first issue of 2016, this journal uses article numbers instead of page numbers. See further details here.

Article Metrics

Back to TopTop