2021
DOI: 10.1021/acs.inorgchem.1c01560
|View full text |Cite
|
Sign up to set email alerts
|

Rational Construction and Performance Regulation of an In(III)–Tetraisophthalate Framework for One-Step Adsorption-Phase Purification of C2H4 from C2 Hydrocarbons

Abstract: The development of porous materials for ethylene (C2H4) separation and purification, a very important separation process in the chemical industry, is urgently needed but quite challenging. In particular, the realization of selectivity-reversed adsorption (namely, C2H4 is not preferentially adsorbed) and the simultaneous capture of multinary coexisting impurities such as ethane (C2H6) and acetylene (C2H2) will significantly simplify process design and reduce energy and cost consumption, but such porous material… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
4
1

Citation Types

3
36
1

Year Published

2021
2021
2024
2024

Publication Types

Select...
8

Relationship

2
6

Authors

Journals

citations
Cited by 51 publications
(40 citation statements)
references
References 74 publications
(110 reference statements)
3
36
1
Order By: Relevance
“…At a gas-phase pressure of 109 kPa, the adsorption selectivity is 3.5 at 298 K, 3.7 at 288 K, and 3.9 at 278 K for a 1:99 C 2 H 2 −C 2 H 4 binary mixture. The values surpass or are comparable to those of some documented MOFs such as Dy-MOF (1.1), 54 ZJNU-14 (1.59), 55 ZJNU-7 (1.77), 56 ZJNU-115 (2.05), 57 FeMOF-74 (2.08), 29 Cu(TIA) (2.09), 58 NOTT-300 (2.17), 59 UPC-98 (3.1), 60 dia-[Sc(Hpzc)(pzc)] (3.1), 61 M′MOF-2 (3.12), 10 Mg-CUK-1 (3.13), 62 and NUC-19 (4.0). 63 As shown in Figure 3f, Since the pore dimension is larger than the kinetic diameters of the adsorbates considered in this work, different host−guest interactions should be responsible for preferentially adsorbing C 2 H n and CO 2 over CH 4 .…”
Section: Resultssupporting
confidence: 63%
“…At a gas-phase pressure of 109 kPa, the adsorption selectivity is 3.5 at 298 K, 3.7 at 288 K, and 3.9 at 278 K for a 1:99 C 2 H 2 −C 2 H 4 binary mixture. The values surpass or are comparable to those of some documented MOFs such as Dy-MOF (1.1), 54 ZJNU-14 (1.59), 55 ZJNU-7 (1.77), 56 ZJNU-115 (2.05), 57 FeMOF-74 (2.08), 29 Cu(TIA) (2.09), 58 NOTT-300 (2.17), 59 UPC-98 (3.1), 60 dia-[Sc(Hpzc)(pzc)] (3.1), 61 M′MOF-2 (3.12), 10 Mg-CUK-1 (3.13), 62 and NUC-19 (4.0). 63 As shown in Figure 3f, Since the pore dimension is larger than the kinetic diameters of the adsorbates considered in this work, different host−guest interactions should be responsible for preferentially adsorbing C 2 H n and CO 2 over CH 4 .…”
Section: Resultssupporting
confidence: 63%
“…Another important dimension is that the altering of anion pillars (e.g., SiF 6 ) can induce the distortion of pore shapes and the rotation of organic ligands (14,15), thus anionpillared HUMs have emerged as the promising C 2 light hydrocarbon adsorbents for binary separations such as C 2 H 2 /C 2 H 4 (16), C 2 H 2 / CO 2 (17), and C 2 H 4 /C 2 H 6 (18). However, the single-step C 2 H 4 purification from ternary C 2 mixtures has never been achieved in adsorptive separations using anion-pillared HUMs, because the quadrupole moment and kinetic diameter of C 2 H 4 [1.5 × 10 −26 (5,(20)(21)(22)(23)(24)(25)(26)(27).…”
Section: Introductionmentioning
confidence: 99%
“…For example, natural gas (NG) is composed mainly of methane (CH 4 ) but also includes various quantities of CO 2 as well as C 2 hydrocarbons. CO 2 /CH 4 and C 2 /C 1 separations thus present a major step toward NG purification, which avoids pipeline corrosion by acidic CO 2 and recovers C 2 hydrocarbon resources to increase its added values. Apart from NG upgrading, C 2 H 4 purification is also a very important industrial process involving the capture from C 2 H 4 of its competing C 2 analogues, including acetylene (C 2 H 2 ) and ethane (C 2 H 6 ). Due to their similar properties (Table S1), separation of C 2 H 4 from a trinary C 2 hydrocarbon mixture is extremely difficult. In addition, CO 2 as an impurity frequently exists in C 2 hydrocarbons.…”
Section: Introductionmentioning
confidence: 99%
“…In light of the HSAB (hard/soft acid/base) principle, upon coordination with trivalent lanthanide ions, the carboxylate groups serve as coordinating groups, while the pyridinic N atoms remain unbound as the potential sites for adsorbing C 2 H 2 and CO 2 molecules. Besides, the m- terphenyl skeleton favors the construction of a 3D coordination network, provides the resulting framework with rigidity and stability, and creates an aromatic-rich pore environment, a structural requirement considered for selective adsorption of C 2 H 6 in preference to C 2 H 4 . With the ligand at hand, we successfully fabricated a pair of isostructural LOFs via solvothermal reactions with Sm­(III) and Eu­(III) ions.…”
Section: Introductionmentioning
confidence: 99%
See 1 more Smart Citation