2020
DOI: 10.1021/acsami.0c04378
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Micro- and Ultramicroporous Polyaminals for Highly Efficient Adsorption/Separation of C1–C3 Hydrocarbons and CO2 in Natural Gas

Abstract: This paper presents a series of micro- and ultramicroporous polyaminals with BET surface areas up to 1304 m2 g–1, which are prepared from two triazine-based tetraamines and three dialdehydes or monoaldehyde through the A4 + B2 or A4 + B1 aminalization reaction. It is interesting to find that the para-substituted monomers are favorable to force the linking struts apart in the network to generate micropores (1.22 nm), whereas the meta-substituted monomers make the pores in the network squeezed by the twisted lin… Show more

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Cited by 41 publications
(46 citation statements)
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“…As seen in Table , the C 2 H 6 uptake value of 80.2 mg/g obtained by PNOP-1 at a temperature of 273 K far surpasses those of previously reported porous organic polymers under equivalent environmental conditions, such as 49.6–61.3 mg/g for sPI, 32.3–67.2 mg/g for aromatic MPI polymers, and <80 mg/g for mesoporous hydrophobic polymeric organic frameworks (mesoPOFs) . Finally, the PNOPs obtained CH 4 uptake values in the range of 14.6–16.8 mg/g at 273 K and 1 bar, which are comparable with those obtained by previously reported porous organic polymers such as BILP-5 (15 mg/g), ALP-4 (14.3 mg/g), and PAN-m1 (17.1 mg/g) . The results in Table also demonstrate that the CO 2 , C 2 H 6 , and CH 4 adsorption capacities of PNOP-1 are distinctly higher than those of PNOP-2, PNOP-1 shows high nitrogen content and microporous surface areas as well as microporous volume compared with PNOP-2.…”
Section: Resultsmentioning
confidence: 50%
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“…As seen in Table , the C 2 H 6 uptake value of 80.2 mg/g obtained by PNOP-1 at a temperature of 273 K far surpasses those of previously reported porous organic polymers under equivalent environmental conditions, such as 49.6–61.3 mg/g for sPI, 32.3–67.2 mg/g for aromatic MPI polymers, and <80 mg/g for mesoporous hydrophobic polymeric organic frameworks (mesoPOFs) . Finally, the PNOPs obtained CH 4 uptake values in the range of 14.6–16.8 mg/g at 273 K and 1 bar, which are comparable with those obtained by previously reported porous organic polymers such as BILP-5 (15 mg/g), ALP-4 (14.3 mg/g), and PAN-m1 (17.1 mg/g) . The results in Table also demonstrate that the CO 2 , C 2 H 6 , and CH 4 adsorption capacities of PNOP-1 are distinctly higher than those of PNOP-2, PNOP-1 shows high nitrogen content and microporous surface areas as well as microporous volume compared with PNOP-2.…”
Section: Resultsmentioning
confidence: 50%
“…49 Finally, the PNOPs obtained CH 4 uptake values in the range of 14.6−16.8 mg/g at 273 K and 1 bar, which are comparable with those obtained by previously reported porous organic polymers such as BILP-5 (15 mg/g), 50 ALP-4 (14.3 mg/g), 2 and PAN-m1 (17.1 mg/g). 4 The results in Table 2 also demonstrate that the CO 2 , C 2 H 6 , and CH 4 adsorption capacities of PNOP-1 are distinctly higher than those of PNOP-2, PNOP-1 shows high nitrogen content and microporous surface areas as well as microporous volume compared with PNOP-2. The observed CO 2 , C 2 H 6 , and CH 4 adsorption properties of the PNOPs were evaluated further by applying the Clausius− Clapeyron equation to calculate the isosteric enthalpies of adsorption (Q st ) from the CO 2 , C 2 H 6 , and CH 4 adsorption isotherms measured at 273 and 298 K. The results are plotted in Figure 6 as functions of the CO 2 , C 2 H 6 , and CH 4 adsorption capacities of the PNOPs obtained at various pressures in Figure 4.…”
Section: ■ Results and Discussionmentioning
confidence: 80%
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“…In a recent study, Li and Wang investigated a series of microporous and ultramicroporous polyaminal networks (PANs) for the separation of C 1 −C 3 hydrocarbons in natural gas. 47 These PANs have the Brunauer−Emmett−Teller SA in the range of 904−1133 m 2 /g and pore volume in the range of 0.62−0.87 cm 3 /g. At ambient conditions, they reported selectivity of propane over methane in a 10:90 (propane/methane) mixture in the range 129.3−296.3 and selectivity of ethane over methane in a 10:90 (ethane/methane) mixture in the range 16.9−23.1.…”
Section: ■ Results and Discussionmentioning
confidence: 99%
“…For petrochemical industry, light hydrocarbon separation is essential, and offers a variety of necessities related to our life. [1][2][3] Currently, the Traditional purification method of distillation is often employed to separate light hydrocarbons under low-temperature and highpressure conditions. [4][5][6] However, this purification process is generally associated with huge energy consumption, which accelerates the process of depleting global energy resources and exacerbates environmental pollution problems.…”
Section: Introductionmentioning
confidence: 99%