Abstract:Two flexible subcomponents, namely tris(4-formylphenyl)phosphate and tris(2-aminoethyl)amine, are assembled into a tetrapodal [4 + 4] cage depending on the solvent effect. Single-crystal structure analysis reveals that the caivity is surrounded by four phosphate uints. Good selectivity of CO2 adsorption over CH4 is demonstrated by the gas adsorption experiment.
“…Overall, NHD could obviously decrease the energy barrier for the regeneration of carbamate by Reaction II (a) and (b) (Figure S15), which is caused by the solvent effect of NHD. 38,39 Generally, molecular H 2 O has higher polarity than that of NHD, resulting in more stable hydrogen bonds between H 2 O and DMPA. These hydrogen bonds might decrease the electron density around N (DMPA), leading to the reduction in the nucleophilicity or alkalinity of DMPA.…”
Physical solvent is a promising alternative for the phase splitting of solvent to drastically reduce the regeneration energy during CO 2 capture. Here, an aqueous biphasic solvent, optimally composed of 30 wt % polyamine (N, N-dimethylpropylamine, DMPA) and 50 wt % physical solvent (polyethyleneglycol dimethyl ether, NHD), is prepared, which presents high cyclic loading, low regeneration energy, and good stability. L 16 (4 5 ) orthogonal tests are performed to comprehensively evaluate the mass-transfer kinetics and the effect of crucial conditions, verifying the weak effect of NHD solvent on mass transfer. The solvent effect of NHD could decrease the energy barrier of carbamate generation from zwitterions (DMPA + COO − ) to enhance chemical absorption. The low polarity of the NHD solvent provides source motivation and accelerates phase splitting. Time−space resolution distribution of CO 2 capacity is established based on a scale-up separator with 5 L solvent, which supports multiscale force analysis for the various stages during phase splitting. The drag force of the homogeneous cluster was first introduced into separation dynamics, referred to as an important reason for the various splitting behaviors of a scale-up separator.
“…Overall, NHD could obviously decrease the energy barrier for the regeneration of carbamate by Reaction II (a) and (b) (Figure S15), which is caused by the solvent effect of NHD. 38,39 Generally, molecular H 2 O has higher polarity than that of NHD, resulting in more stable hydrogen bonds between H 2 O and DMPA. These hydrogen bonds might decrease the electron density around N (DMPA), leading to the reduction in the nucleophilicity or alkalinity of DMPA.…”
Physical solvent is a promising alternative for the phase splitting of solvent to drastically reduce the regeneration energy during CO 2 capture. Here, an aqueous biphasic solvent, optimally composed of 30 wt % polyamine (N, N-dimethylpropylamine, DMPA) and 50 wt % physical solvent (polyethyleneglycol dimethyl ether, NHD), is prepared, which presents high cyclic loading, low regeneration energy, and good stability. L 16 (4 5 ) orthogonal tests are performed to comprehensively evaluate the mass-transfer kinetics and the effect of crucial conditions, verifying the weak effect of NHD solvent on mass transfer. The solvent effect of NHD could decrease the energy barrier of carbamate generation from zwitterions (DMPA + COO − ) to enhance chemical absorption. The low polarity of the NHD solvent provides source motivation and accelerates phase splitting. Time−space resolution distribution of CO 2 capacity is established based on a scale-up separator with 5 L solvent, which supports multiscale force analysis for the various stages during phase splitting. The drag force of the homogeneous cluster was first introduced into separation dynamics, referred to as an important reason for the various splitting behaviors of a scale-up separator.
“…Generally speaking, the larger the difference in size, the more easily separation can be achieved. Therefore, the separation of gas pairs with a relatively profound size difference, such as CO 2 / N 2 34,35 and CO 2 /CH 4 , 36,37 is straightforward using POCs.…”
Section: Separation Of Gases With a Small Size Differencementioning
confidence: 99%
“…Many studies have reported the ideal selectivity in gas pairs of CO 2 /N 2 or CO 2 /CH 4 achieved by POCs; the ideal selectivity value of the CO 2 /N 2 pair ranges from B10 to 200, 34,35,[38][39][40][41][42] at standard temperatures (273-298 K) and pressure (1 bar), whereas the reported selectivity of CO 2 /CH 4 ranges from B4 to B50. [36][37][38] The real challenge for separation is gas pairs with a small size difference. In Fig.…”
Section: Separation Of Gases With a Small Size Differencementioning
Porous organic cages (POCs) have emerged as a new sub-class of porous materials that stand out by virtue of their tunability, modularity, and processibility. Similar to other porous materials such...
“…Huang et al recently reported profound solvent effect in the formation of OICs from trisformyl 6 and 1 . [ 12 ] When the reaction was carried out in MeCN with 1:1 molar ratio [2+3] imine cage 7 was obtained with characteristic peaks in ESI‐MS and 1 H NMR spectroscopy. But replacement of MeCN by CHCl 3 led to complete change of framework toward [4+4] imine cage 8 (Scheme 3).…”
Section: Aliphatic Triamine Based Oics: Syntheses Special Featurementioning
Molecules bearing three primary amine groups are ubiquitous substances in various fields of synthetic chemistry. Some of them are commercially available and the rests are emerged from the designed protocols of synthetic chemists. It has been observed that such aliphatic as well as aromatic triamines are excellent precursors for the design and synthesis of various cage molecules of which organic imine cages (OICs) and related amine macrocycles belong to the category of special interest. These compounds possess unique architectures and already made their marks in the field of supramolecular chemistry, synthetic methodology, and material science. In this review we aimed to consider recent reports that highlighted the syntheses, special features, and applications of primary triamine based OICs and related amine macrocycles.
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