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Zeolites and Porous Materials: Synthesis, Properties and Applications

A special issue of Molecules (ISSN 1420-3049). This special issue belongs to the section "Inorganic Chemistry".

Deadline for manuscript submissions: closed (30 June 2024) | Viewed by 32949

Special Issue Editors


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Guest Editor
School of Environment and Chemical Engineering, Foshan University, Foshan, China
Interests: porous materials; MOFs; activated carbon; adsorption; separation; VOCs

E-Mail Website
Guest Editor
School of Chemical Engineering and Light Industry, Guangdong University of Technology, Guangzhou, China
Interests: zeolites; catalysis; diffusion; alkylation; functionalization

Special Issue Information

Dear Colleagues,

Since the invention of synthetic zeolite in 1959, the innovation of porous materials has played an important role in industrial production. The porous material is a kind of material with a network structure composed of interconnected or closed holes. Because of its large specific surface area and porosity, good chemical properties, photoelectric properties, mechanical properties, adsorption properties, and permeability properties, it is widely used in industrial production and life. With the continuous development of materials science, the types of porous materials are increasing, including natural porous materials, molecular sieve, novel carbon materials (carbon molecular sieve, super activated carbon, carbon fiber, carbon nanotubes, etc.), porous metal materials, metal-organic frameworks, covalent organic frameworks, hydrogen-bonded organic frameworks, etc. As a new type of functional material, porous materials have a wide range of applications in the fields of gas adsorption and separation, catalysis, fluorescence, sensor, etc.

We would like to invite you to contribute to this Special Issue of Molecules titled “Zeolites and Porous Materials: Synthesis, Properties and Applications”. Your valuable research articles and reviews can find a worldwide audience among readers of Molecules.

Dr. Feng Xu
Prof. Dr. Baoyu Liu
Guest Editors

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Keywords

  • porous materials
  • zeolites
  • MOFs
  • synthesis
  • properties
  • applications

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Published Papers (13 papers)

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14 pages, 44406 KiB  
Article
Engineering In-Co3O4/H-SSZ-39(OA) Catalyst for CH4-SCR of NOx: Mild Oxalic Acid (OA) Leaching and Co3O4 Modification
by Guanyu Chen, Weixin Zhang, Rongshu Zhu, Yanpeng Chen, Minghu Zhao and Mei Hong
Molecules 2024, 29(16), 3747; https://doi.org/10.3390/molecules29163747 - 7 Aug 2024
Cited by 1 | Viewed by 883
Abstract
Zeolite-based catalysts efficiently catalyze the selective catalytic reduction of NOx with methane (CH4-SCR) for the environmentally friendly removal of nitrogen oxides, but suffer severe deactivation in high-temperature SO2- and H2O-containing flue gas. In this work, SSZ-39 [...] Read more.
Zeolite-based catalysts efficiently catalyze the selective catalytic reduction of NOx with methane (CH4-SCR) for the environmentally friendly removal of nitrogen oxides, but suffer severe deactivation in high-temperature SO2- and H2O-containing flue gas. In this work, SSZ-39 zeolite (AEI topology) with high hydrothermal stability is reported for preparing CH4-SCR catalysts. Mild acid leaching with oxalic acid (OA) not only modulates the Si/Al ratio of commercial SSZ-39 to a suitable value, but also removes some extra-framework Al atoms, introducing a small number of mesopores into the zeolite that alleviate diffusion limitation. Additional Co3O4 modification during indium exchange further enhances the catalytic activity of the resulting In-Co3O4/H-SSZ-39(OA). The optimized sample exhibits remarkable performance in CH4-SCR under a gas hourly space velocity (GHSV) of 24,000 h−1 and in the presence of 5 vol% H2O. Even under harsh SO2- and H2O-containing high-temperature conditions, it shows satisfactory stability. Catalysts containing Co3O4 components demonstrate much higher CH4 conversion. The strong mutual interaction between Co3O4 and Brønsted acid sites, confirmed by the temperature-programmed desorption of NO (NO-TPD), enables more stable NxOy species to be retained in In-Co3O4/H-SSZ-39(OA) to supply further reactions at high temperatures. Full article
(This article belongs to the Special Issue Zeolites and Porous Materials: Synthesis, Properties and Applications)
Show Figures

Figure 1

Figure 1
<p>Effects of oxalic acid concentration, etching time, and etching temperature in acid etching post-treatment on the (<b>a</b>–<b>c</b>) NO<span class="html-italic"><sub>x</sub></span> conversion, (<b>d</b>–<b>f</b>) CH<sub>4</sub> conversion, and (<b>g</b>–<b>i</b>) CH<sub>4</sub> selectivity of the resulting catalysts for dry CH<sub>4</sub>-SCR. Reaction conditions: [NO] = 400 ppm, [CH<sub>4</sub>] = 600 ppm, [O<sub>2</sub>] = 10 vol%, Ar balance, GHSV = 24,000 h<sup>−1</sup>.</p>
Full article ">Figure 2
<p>Effect of the Co<sub>3</sub>O<sub>4</sub> to H-SSZ-39(OA) mass ratio on the (<b>a</b>) NO<span class="html-italic"><sub>x</sub></span> conversion and (<b>b</b>) CH<sub>4</sub> conversion of the resulting catalysts under wet conditions. Reaction conditions: [NO] = 400 ppm, [CH<sub>4</sub>] = 600 ppm, [O<sub>2</sub>] = 10 vol%, [H<sub>2</sub>O] = 5 vol%, Ar balance, GHSV = 24,000 h<sup>−1</sup>. (<b>c</b>) Recyclability test of In-Co<sub>3</sub>O<sub>4</sub>/H-SSZ-39(OA) under harsh H<sub>2</sub>O- and SO<sub>2</sub>-containing conditions. Reaction conditions: [NO] = 400 ppm, [CH<sub>4</sub>] = 600 ppm, [O<sub>2</sub>] = 10 vol%, [H<sub>2</sub>O] = 5 vol%, [SO<sub>2</sub>] = 50 ppm, Ar balance, GHSV = 12,000 h<sup>−1</sup>. (<b>d</b>) Stability test of In-Co<sub>3</sub>O<sub>4</sub>/H-SSZ-39(OA) under harsh H<sub>2</sub>O- and SO<sub>2</sub>-containing conditions. Reaction conditions: [NO] = 400 ppm, [CH<sub>4</sub>] = 600 ppm, [O<sub>2</sub>] = 10 vol%, [H<sub>2</sub>O] = 5 vol%, [SO<sub>2</sub>] = 50 ppm, Ar balance, GHSV = 12,000 h<sup>−1</sup>, <span class="html-italic">T</span> = 600 °C.</p>
Full article ">Figure 3
<p>SEM images of (<b>a</b>) Pristine H-SSZ-39, (<b>b</b>) In/H-SSZ-39(OA), and (<b>c</b>) In-Co<sub>3</sub>O<sub>4</sub>/H-SSZ-39(OA). HRTEM images of (<b>d</b>) Pristine H-SSZ-39, (<b>e</b>) In/H-SSZ-39(OA), and (<b>f</b>) In-Co<sub>3</sub>O<sub>4</sub>/H-SSZ-39(OA). (<b>g</b>) PXRD patterns, (<b>h</b>) N<sub>2</sub> adsorption–desorption isotherms, and (<b>i</b>) NLDFT PSD curves of samples.</p>
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<p>(<b>a</b>) <sup>27</sup>Al MAS SSNMR and (<b>b</b>) <sup>29</sup>Si MAS SSNMR of Pristine H-SSZ-39 and In/H-SSZ-39(OA).</p>
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<p>High-resolution XPS spectra of (<b>a</b>) In 3d region and (<b>b</b>) Co 2p region.</p>
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<p>(<b>a</b>) NH<sub>3</sub>-TPD profiles and (<b>b</b>) NO-TPD profiles of samples.</p>
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15 pages, 2677 KiB  
Article
Adsorption of Bichromate and Arsenate Anions by a Sorbent Based on Bentonite Clay Modified with Polyhydroxocations of Iron and Aluminum by the “Co-Precipitation” Method
by Bakytgul Kussainova, Gaukhar Tazhkenova, Ivan Kazarinov, Marina Burashnikova, Aisha Nurlybayeva, Gulnaziya Seitbekova, Saule Kantarbayeva, Nazgul Murzakasymova, Elvira Baibazarova, Dinara Altynbekova, Assem Shinibekova and Aidana Bazarkhankyzy
Molecules 2024, 29(15), 3709; https://doi.org/10.3390/molecules29153709 - 5 Aug 2024
Cited by 1 | Viewed by 968
Abstract
The physicochemical properties of natural bentonite and its sorbents were studied. It has been established the modification of natural bentonites using polyhydroxoxides of iron (III) (mod.1_Fe_5-c) and aluminum (III) (mod.1_Al_5-c) by the “co-precipitation” method led to changes in their chemical composition, structure, and [...] Read more.
The physicochemical properties of natural bentonite and its sorbents were studied. It has been established the modification of natural bentonites using polyhydroxoxides of iron (III) (mod.1_Fe_5-c) and aluminum (III) (mod.1_Al_5-c) by the “co-precipitation” method led to changes in their chemical composition, structure, and sorption properties. It was shown that modified sorbents based on natural bentonite are finely porous (nanostructured) objects with a predominance of pores of 1.5–8.0 nm in size. The modification of bentonite with iron (III) and aluminum compounds by the “co-precipitation” method also leads to an increase in the sorption capacity of the obtained sorbents with respect to bichromate and arsenate anions. A kinetic analysis showed that, at the initial stage, the sorption process was controlled by an external diffusion factor, that is, the diffusion of the sorbent from the solution to the liquid film on the surface of the sorbent. The sorption process then began to proceed in a mixed diffusion mode when it limited both the external diffusion factor and the intra-diffusion factor (diffusion of the sorbent to the active centers through the system of pores and capillaries). To clarify the contribution of the chemical stage to the rate of adsorption of bichromate and arsenate anions by the sorbents under study, kinetic curves were processed using equations of chemical kinetics (pseudo-first-order, pseudo-second-order, and Elovich models). It was found that the adsorption of the studied anions by the modified sorbents based on natural bentonite was best described by a pseudo-second-order kinetic model. The high value of the correlation coefficient for the Elovich model (R2 > 0.9) allows us to conclude that there are structural disorders in the porous system of the studied sorbents, and their surfaces can be considered heterogeneous. Considering that heterogeneous processes occur on the surface of the sorbent, it is natural that all surface properties (structure, chemical composition of the surface layer, etc.) play an important role in anion adsorption. Full article
(This article belongs to the Special Issue Zeolites and Porous Materials: Synthesis, Properties and Applications)
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Figure 1

Figure 1
<p>X-ray diffraction patterns of the examined sorbents derived from natural bentonite from the Pogodayevo deposit (Kazakhstan): 1—mod.1; 2—mod.1_Al_5-c; 3—mod.1_Fe_5-c, where <span class="html-fig-inline" id="molecules-29-03709-i001"><img alt="Molecules 29 03709 i001" src="/molecules/molecules-29-03709/article_deploy/html/images/molecules-29-03709-i001.png"/></span>—montmorillonite; □—α-cristobalite; ■—plagioclase.</p>
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<p>Kinetic curves of the adsorption process of bichromate (<b>a</b>) and arsenate anions (<b>b</b>) by the studied modified sorbents in a neutral medium.</p>
Full article ">Figure 2 Cont.
<p>Kinetic curves of the adsorption process of bichromate (<b>a</b>) and arsenate anions (<b>b</b>) by the studied modified sorbents in a neutral medium.</p>
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<p>Adsorption isotherms in a neutral medium of (<b>a</b>) bichromate and (<b>b</b>) arsenate anions on the obtained sorbents.</p>
Full article ">Figure 3 Cont.
<p>Adsorption isotherms in a neutral medium of (<b>a</b>) bichromate and (<b>b</b>) arsenate anions on the obtained sorbents.</p>
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<p>Isotherms of adsorption of (<b>a</b>) bichromate and (<b>b</b>) arsenate anions by the studied sorbents, represented in inverse coordinates in accordance with the Langmuir Equation (3).</p>
Full article ">Figure 5
<p>Dependence of –<span class="html-italic">ln</span>(1 − <span class="html-italic">F</span>) on t (spring diffusion model) during adsorption of bichromate and arsenate anions by bentonite and modified iron(III) and aluminum polyhydroxocations by bentonite-based sorbents: (<b>a</b>) bichromate anion; (<b>b</b>) arsenate anion.</p>
Full article ">Figure 6
<p>Dependence of qt on <span class="html-italic">t</span><sup>0.5</sup> (internal diffusion model) during adsorption of bichromate and arsenate anions by bentonite and modified iron (III) and aluminum polyhydroxocations by bentonite-based sorbents: (<b>a</b>) bichromate anion; (<b>b</b>) arsenate anion.</p>
Full article ">Figure 7
<p>Dependence of <span class="html-italic">ln</span>(<span class="html-italic">q<sub>e</sub></span> − <span class="html-italic">q<sub>t</sub></span>) on <span class="html-italic">t</span> (a pseudo-first-order kinetic model) during adsorption of bichromate and arsenate anions by bentonite and modified iron (III) and aluminum polyhydroxocations by bentonite-based sorbents: (<b>a</b>) bichromate anion; (<b>b</b>) arsenate anion.</p>
Full article ">Figure 8
<p>Dependence of <span class="html-italic">t</span>/<span class="html-italic">q<sub>t</sub></span> on <span class="html-italic">t</span> (kinetic model of pseudo-second-order) during adsorption of bichromate and arsenate anions by bentonite and modified iron (III) and aluminum polyhydroxocations by bentonite-based sorbents: (<b>a</b>) bichromate anion; (<b>b</b>) arsenate anion.</p>
Full article ">Figure 9
<p>Dependence of <span class="html-italic">t</span>/<span class="html-italic">q<sub>t</sub></span> on <span class="html-italic">t</span> (Elovich model) during adsorption of bichromate and arsenate anions by bentonite and modified iron (III) and aluminum polyhydroxocations by bentonite-based sorbents: (<b>a</b>) bichromate–anion (<b>b</b>) arsenate anion.</p>
Full article ">
22 pages, 3957 KiB  
Article
Encapsulation of Imidazole into Ce-Modified Mesoporous KIT-6 for High Anhydrous Proton Conductivity
by Agata Tabero, Aldona Jankowska, Adam Ostrowski, Ewa Janiszewska, Jolanta Kowalska-Kuś, Agnieszka Held and Stanisław Kowalak
Molecules 2024, 29(13), 3239; https://doi.org/10.3390/molecules29133239 - 8 Jul 2024
Cited by 1 | Viewed by 905
Abstract
Imidazole molecules entrapped in porous materials can exhibit high and stable proton conductivity suitable for elevated temperature (>373 K) fuel cell applications. In this study, new anhydrous proton conductors based on imidazole and mesoporous KIT-6 were prepared. To explore the impact of the [...] Read more.
Imidazole molecules entrapped in porous materials can exhibit high and stable proton conductivity suitable for elevated temperature (>373 K) fuel cell applications. In this study, new anhydrous proton conductors based on imidazole and mesoporous KIT-6 were prepared. To explore the impact of the acidic nature of the porous matrix on proton conduction, a series of KIT-6 materials with varying Si/Al ratios and pure silica materials were synthesized. These materials were additionally modified with cerium atoms to enhance their Brønsted acidity. TPD-NH3 and esterification model reaction confirmed that incorporating aluminum into the silica framework and subsequent modification with cerium atoms generated additional acidic sites. UV-Vis and XPS identified the presence of Ce3+ and Ce4+ in the KIT-6 materials, indicating that high-temperature treatment after cerium introduction may lead to partial cerium incorporation into the framework. EIS studies demonstrated that dispersing imidazole within the KIT-6 matrices resulted in composites showing high proton conductivity over a wide temperature range (300–393 K). The presence of weak acidic centers, particularly Brønsted sites, was found to be beneficial for achieving high conductivity. Cerium-modified composites exhibited conductivity surpassing that of molten imidazole, with the highest conductivity (1.13 × 10−3 S/cm at 393 K) recorded under anhydrous conditions for Ce-KIT-6. Furthermore, all tested composites maintained high stability over multiple heating and cooling cycles. Full article
(This article belongs to the Special Issue Zeolites and Porous Materials: Synthesis, Properties and Applications)
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Graphical abstract

Graphical abstract
Full article ">Figure 1
<p>PXRD patterns of KIT-6 matrices with different Si/Al ratio: 25; 50; 100; 200; and infinity.</p>
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<p>N<sub>2</sub> adsorption/desorption isotherms (<b>A</b>) and pore size distribution (<b>B</b>) of KIT-6 materials.</p>
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<p>FTIR spectra of selected H-KIT-6 and Ce-KIT-6 samples with different Si/Al ratio.</p>
Full article ">Figure 4
<p>UV-Vis spectra of selected Ce-KIT-6 materials before (<b>A</b>) and after calcination at 673 K (<b>B</b>).</p>
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<p>TEM images of H-KIT-6 (100) (<b>A</b>) and Ce-KIT-6 (100) (<b>B</b>) samples.</p>
Full article ">Figure 6
<p>XPS spectrum of the Ce3d core level of Ce-KIT-6 (100).</p>
Full article ">Figure 7
<p>Temperature dependence of conductivity measured during the second cooling cycle for imidazole and imidazole-containing H-KIT-6 composites of various Im loading.</p>
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<p>Temperature dependence of conductivity measured during the second cooling cycle for imidazole and imidazole-containing Ce-KIT-6 composites of various Im loading.</p>
Full article ">Figure 9
<p>Temperature dependence of conductivity for the H-KIT-6 (100) 0.40 Im composite recorded for two heating–cooling cycles.</p>
Full article ">Figure 10
<p>Temperature dependence of conductivity for the Ce-KIT-6 (100) 0.40 Im composite recorded for two heating–cooling cycles.</p>
Full article ">Figure 11
<p>Temperature dependence of conductivity and activation energies for H-KIT-6 composites with different Si/Al ratios measured during the second cooling cycle.</p>
Full article ">Figure 12
<p>Temperature dependence of conductivity and activation energies for Ce-KIT-6 composites with different Si/Al ratios measured during the second cooling cycle.</p>
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<p>Conductivity values of selected composites determined at 393 K for second cooling cycle.</p>
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<p>Correlation of conductivity values of selected composites determined at 393 K for second cooling cycle with acetic acid (HAc) conversion.</p>
Full article ">
16 pages, 3623 KiB  
Article
High Reactivity of Dimethyl Ether Activated by Zeolite Ferrierite within a Fer Cage: A Prediction Study
by Xiaofang Chen, Pei Feng and Xiujie Li
Molecules 2024, 29(9), 2000; https://doi.org/10.3390/molecules29092000 - 26 Apr 2024
Viewed by 888
Abstract
The zeolite-catalyzed conversion of DME into chemicals is considered environmentally friendly in industry. The periodic density functional theory, statistical thermodynamics, and the transition state theory are used to study some possible parallel reactions about the hydrogen-bonded DME over zeolite ferrierite. The following are [...] Read more.
The zeolite-catalyzed conversion of DME into chemicals is considered environmentally friendly in industry. The periodic density functional theory, statistical thermodynamics, and the transition state theory are used to study some possible parallel reactions about the hydrogen-bonded DME over zeolite ferrierite. The following are the key findings: (1) the charge separation probably leads to the conversion of a hydrogen-bonded DME into a dimethyl oxonium ion (i.e., DMO+ or (CH3)2OH+) with a positive charge of about 0.804 e; (2) the methylation of DME, CH3OH, H2O, and CO by DMO+ at the T2O6 site of zeolite ferrierite shows the different activated internal energy (∆E) ranging from 18.47 to 30.06 kcal/mol, implying the strong methylation ability of DMO+; (3) H-abstraction by DMO+ is about 3.94–15.53 or 6.57–18.16 kcal/mol higher than DMO+ methylation in the activation internal energy; (4) six DMO+-mediated reactions are more likely to occur due to the lower barriers, compared to the experimental barrier (i.e., 39.87 kcal/mol) for methyl acetate synthesis; (5) active intermediates, such as (CH3)3O+, (CH3)2OH+, CH3CO+, CH3OH2+, and CH2=OH+, are expected to appear; (6) DMO+ is slightly weaker than the well-known surface methoxy species (ZO-CH3) in methylation; and (7) the methylated activity declines in the order of DME, CH3OH, H2O, and CO, with corresponding rate constants at 463.15 K of about 3.4 × 104, 1.1 × 102, 0.18, and 8.2 × 10−2 s−1, respectively. Full article
(This article belongs to the Special Issue Zeolites and Porous Materials: Synthesis, Properties and Applications)
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Graphical abstract

Graphical abstract
Full article ">Figure 1
<p>Dimethyl ester (DME) adsorbed at the T2O6 site of zeolite ferrierite within the eight-membered ring (8MR) channel: (<b>a</b>) parallel to and (<b>b</b>) perpendicular to the [010] plane. Noting that (1) O in red, Si in yellow, Al in pink, C in grey, and H in white; (2) grey lines for interconnecting atoms away from the 8MR, and (3) the blue number is the distance (in Å) between two atoms.</p>
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<p>Within a fer cage of zeolite ferrierite, an attacking molecule (R1-A-R2) is methylated by a hydrogen-bonded DME molecule (i.e., DMO<sup>+</sup>) at the T2O6 site (in a blue dash square). Notes: (1) O in red, Si in yellow, Al in pink, C in grey, and H in white, and grey lines for interconnecting atoms and bonds away from the fer cage; (2) DME: A = O, R1 = R2 = CH<sub>3</sub>; (3) CH<sub>3</sub>OH: A = O, R1 = CH<sub>3</sub>, R2 = H; (4) H<sub>2</sub>O: A = O, R1 = R2 = H; (5) CO: A = C, R1 = O, and R2 is omitted; (6) H<sub>Z</sub>, O<sub>D</sub>, C<sub>M</sub>, and A are the Brönsted acid proton, O atom of DME, the migrant C atom, and target A atom, and (7) the black arrow is the main direction of atom movement.</p>
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<p>Some distances (<b>d</b>) and angles (∠) in the reactant (Rex), the transition state (TSx), and the product (Px) of Equation (x) (x = 1–4) in the <a href="#sec1-molecules-29-02000" class="html-sec">Section 1</a>: (<b>a</b>) d(O6-H<sub>Z</sub>), (<b>b</b>) d(H<sub>Z</sub>-O<sub>D</sub>), (<b>c</b>) d(O<sub>D</sub>-C<sub>M</sub>), (<b>d</b>) d(C<sub>M</sub>-A), (<b>e</b>) ∠O<sub>D</sub>C<sub>M</sub>A, and (<b>f</b>) ∠H<sub>Z</sub>OC<sub>M</sub>A. Notes: (1) O6, H<sub>Z</sub>, O<sub>D</sub>, and C<sub>M</sub> are the framework O6 atom and the BA proton of zeolite ferrierite, and the O atom and the migrant C atom of the hydrogen-bonded DME (i.e., DMO<sup>+</sup>); (2) A is the O atom of DME, CH<sub>3</sub>OH or H<sub>2</sub>O moiety, yet it is the C atom of CO moiety; (3) Each color represents the species in one chemical equation.</p>
Full article ">Figure 4
<p>Calculated energy profile for DMO<sup>+</sup> methylation and H-abstraction at T2O6 site of zeolite ferrierite within a fer cage. For Equations (1)–(6), please refer to the <a href="#sec1-molecules-29-02000" class="html-sec">Section 1</a>.</p>
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<p>The hydrogen-bonded DME (in blue dash square) abstracts one of methyl H atoms of attracting molecules (i.e., DME or CH<sub>3</sub>OH) at the T2O6 site within a fer cage of zeolite ferrierite. Notes: (1) O in red, Si in yellow, Al in pink, C in grey, and H in white, grey lines for interconnecting atoms and bonds away from the fer cage; (2) for DME, R = -CH<sub>3</sub>; for CH<sub>3</sub>OH, R = H; (3) O<sub>D</sub>, C<sub>M</sub>, and H<sub>M</sub> are the O atom and the migrant methyl C atom of hydrogen-bonded DME, and the migrant methyl H atom of attracking molecules, and (4) the black arrow is the main direction of atom movement of interest.</p>
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<p>Rate constants (k<sub>x</sub>) for DMO<sup>+</sup> methylation (x = 1–4) and DMO<sup>+</sup> H-abstraction (x = 5–6), and the experimental synthesis of methyl acetate (k<sub>exp</sub>).</p>
Full article ">Scheme 1
<p>Lone electrons in (<b>a</b>) DME, CH<sub>3</sub>OH, and H<sub>2</sub>O, and (<b>b</b>) CO. Notes: (1) for DME, R1 = R2 = -CH<sub>3</sub>; (2) for CH<sub>3</sub>OH, R1 = CH<sub>3</sub>, R2 = H; (3) for H<sub>2</sub>O, R1 = R2 = H; (4) a red or black dot represents an electron from the O or C atom.</p>
Full article ">Scheme 2
<p>A fer cage (highlights in ball and stick) within the T2O6 configuration of the acidic zeolite ferrierite (H-FER). Note that grey lines stand for interconnecting atoms and bonds away from the fer cage.</p>
Full article ">
14 pages, 6566 KiB  
Article
A Polyzwitterionic@MOF Hydrogel with Exceptionally High Water Vapor Uptake for Efficient Atmospheric Water Harvesting
by Jian Yan, Wenjia Li, Yingyin Yu, Guangyu Huang, Junjie Peng, Daofei Lv, Xin Chen, Xun Wang and Zewei Liu
Molecules 2024, 29(8), 1851; https://doi.org/10.3390/molecules29081851 - 18 Apr 2024
Cited by 2 | Viewed by 1682
Abstract
Atmospheric water harvesting (AWH) is considered a promising strategy for sustainable freshwater production in landlocked and arid regions. Hygroscopic salt-based composite sorbents have attracted widespread attention for their water harvesting performance, but suffer from aggregation and leakage issues due to the salting-out effect. [...] Read more.
Atmospheric water harvesting (AWH) is considered a promising strategy for sustainable freshwater production in landlocked and arid regions. Hygroscopic salt-based composite sorbents have attracted widespread attention for their water harvesting performance, but suffer from aggregation and leakage issues due to the salting-out effect. In this study, we synthesized a PML hydrogel composite by incorporating zwitterionic hydrogel (PDMAPS) and MIL-101(Cr) as a host for LiCl. The PML hydrogel was characterized using various techniques including X-ray diffraction (XRD), scanning electron microscopy (SEM), Fourier transform infrared (FTIR), and thermogravimetric analysis (TGA). The swelling properties and water vapor adsorption-desorption properties of the PML hydrogel were also assessed. The results demonstrate that the MIL-101(Cr) was uniformly embedded into PDMAP hydrogel, and the PML hydrogel exhibits a swelling ratio of 2.29 due to the salting-in behavior. The PML hydrogel exhibited exceptional water vapor sorption capacity of 0.614 g/g at 298 K, RH = 40% and 1.827 g/g at 298 K, RH = 90%. It reached 80% of its saturated adsorption capacity within 117 and 149 min at 298 K, RH = 30% and 90%, respectively. Additionally, the PML hydrogel showed excellent reversibility in terms of water vapor adsorption after ten consecutive cycles of adsorption-desorption. The remarkable adsorption capacity, favorable adsorption-desorption rate, and regeneration stability make the PML hydrogel a potential candidate for AWH. This polymer-MOF synergistic strategy for immobilization of LiCl in this work offers new insights into designing advanced materials for AWH. Full article
(This article belongs to the Special Issue Zeolites and Porous Materials: Synthesis, Properties and Applications)
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<p>Diagram of (<b>a</b>) PML hydrogel. (<b>b</b>) Primary components of PML hydrogel. (<b>c</b>) Schematic of the fabrication process of PDMAPS, PL, and PML hydrogels.</p>
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<p>The optical photograph of (<b>a</b>) dried PL, (<b>b</b>) wet PL, (<b>c</b>) dried PML, and (<b>d</b>) wet PML hydrogel after swelling in DI water. (<b>e</b>) Swelling ratio of PL and PML hydrogels in DI water.</p>
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<p>XRD patterns of PDMAPS, PML hydrogels, and MIL-101(Cr).</p>
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<p>SEM images of (<b>a</b>) PDMAPS, (<b>b</b>,<b>c</b>) PL, (<b>d</b>,<b>e</b>) PDMAPS/MIL-101, and (<b>f</b>) PML hydrogels.</p>
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<p>FTIR spectra of PDMAPS, PL, PML hydrogels, and MIL-101(Cr).</p>
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<p>Thermogravimetric analysis of PDMAPS, PL, PML hydrogels, and LiCl.</p>
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<p>Water vapor adsorption isotherms at 298 K on PL hydrogel with different LiCl content.</p>
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<p>Adsorption isotherms of water vapor on PDMAPS, PL, PML hydrogels, and MIL-101(Cr)/LiCl at 298 K.</p>
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<p>Adsorption kinetics of water vapor on the PDMAPS, PL, PML hydrogels at 298 K, RH = 30% (<b>a</b>) and 90% (<b>b</b>).</p>
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<p>Kinetic curves of fractional transient uptakes of water vapor on the PDMAPS, PL, PML hydrogels at 298 K, RH = 30% (<b>a</b>) and 90% (<b>b</b>).</p>
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<p>Desorption kinetics of water vapor on the PML hydrogel at 353 K, RH = 0%.</p>
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<p>Water vapor adsorption-desorption cycles on the PML hydrogel at 298 K, RH = 90% (adsorption) and 353 K, RH = 0% (desorption).</p>
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14 pages, 6302 KiB  
Article
Study of CHF3/CH2F2 Adsorption Separation in TIFSIX-2-Cu-i
by Shoudong Wang, Lei Zhou, Hongyun Qin, Zixu Dong, Haoyuan Li, Bo Liu, Zhilu Wang, Lina Zhang, Qiang Fu and Xia Chen
Molecules 2024, 29(8), 1721; https://doi.org/10.3390/molecules29081721 - 11 Apr 2024
Viewed by 1019
Abstract
Hydrofluorocarbons (HFCs) have important applications in different industries; however, they are environmentally unfriendly due to their high global warming potential (GWP). Hence, reclamation of used hydrofluorocarbons via energy-efficient adsorption-based separation will greatly contribute to reducing their impact on the environment. In particular, the [...] Read more.
Hydrofluorocarbons (HFCs) have important applications in different industries; however, they are environmentally unfriendly due to their high global warming potential (GWP). Hence, reclamation of used hydrofluorocarbons via energy-efficient adsorption-based separation will greatly contribute to reducing their impact on the environment. In particular, the separation of azeotropic refrigerants remains challenging, such as typical mixtures of CH2F2 (HFC-23) and CHF3 (HFC-32), due to a lack of adsorptive mechanisms. Metal–organic frameworks (MOFs) can provide a promising solution for the separation of CHF3–CH2F2 mixtures. In this study, the adsorption mechanism of CHF3–CH2F2 mixtures in TIFSIX-2-Cu-i was revealed at the microscopic level by combining static pure-component adsorption experiments, molecular simulations, and density-functional theory (DFT) calculations. The adsorption separation selectivity of CH2F2/CHF3 in TIFSIX-2-Cu-i is 3.17 at 3 bar under 308 K. The existence of similar TiF62− binding sites for CH2F2 or CHF3 was revealed in TIFSIX-2-Cu-i. Interactions between the fluorine atom of the framework and the hydrogen atom of the guest molecule were found to be responsible for determining the high adsorption separation selectivity of CH2F2/CHF3. This exploration is important for the design of highly selective adsorbents for the separation of azeotropic refrigerants. Full article
(This article belongs to the Special Issue Zeolites and Porous Materials: Synthesis, Properties and Applications)
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<p>The experimental and simulated adsorption isotherms for pure CHF<sub>3</sub> (<b>a</b>) or CH<sub>2</sub>F<sub>2</sub> (<b>b</b>) at 288, 298, and 308 K in TIFSIX-2-Cu-i.</p>
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<p>The adsorption separation selectivity for CH<sub>2</sub>F<sub>2</sub> over CHF<sub>3</sub> in TIFSIX-2-Cu-i at different temperatures and pressures, which correspond to the CH<sub>2</sub>F<sub>2</sub>-CHF<sub>3</sub> mixture (CH<sub>2</sub>F<sub>2</sub>/CHF<sub>3</sub>, 50/50, <span class="html-italic">v</span>/<span class="html-italic">v</span>).</p>
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<p>The isosteric adsorption heat (Qst) of CH<sub>2</sub>F<sub>2</sub>/CHF<sub>3</sub> on the TIFSIX-2-Cu-i.</p>
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<p>Mean-square displacements for CHF<sub>3</sub>–CH<sub>2</sub>F<sub>2</sub> mixture (CHF<sub>3</sub>/CH<sub>2</sub>F<sub>2</sub>, 50/50, <span class="html-italic">v</span>/<span class="html-italic">v</span>) in TIFSIX-2-Cu-i at 288 K (<b>a</b>), 298 K (<b>b</b>), and 308 K (<b>c</b>).</p>
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<p>The typical binding sites for CH<sub>2</sub>F<sub>2</sub> (<b>a</b>) or CHF<sub>3</sub> (<b>b</b>) in TIFSIX-2-Cu-i. The cyan, gray, and white spheres represent fluorine, carbon, and hydrogen atoms, respectively.</p>
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<p>The RDF between the framework and each atom of CHF<sub>3</sub> (<b>a</b>)/CH<sub>2</sub>F<sub>2</sub> (<b>b</b>); the RDF between the representative atoms on the framework and hydrogen atom of CHF<sub>3</sub> (<b>c</b>)/CH<sub>2</sub>F<sub>2</sub> (<b>d</b>) in 298 K.</p>
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<p>The redistribution of charge density in TIFSIX-2-Cu-i after adsorbing CHF<sub>3</sub> molecules (<b>a</b>) or CH<sub>2</sub>F<sub>2</sub> molecules (<b>b</b>). Color code: brown, C; meat pink, H; silver, F; blue, Ti.</p>
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<p>The slices of charge density redistribution for TIFSIX-2-Cu-i and CHF<sub>3</sub> (<b>a</b>)/CH<sub>2</sub>F<sub>2</sub> (<b>b</b>) after molecular adsorption, which correspond to the electron transfer between hydrogen atom of CHF<sub>3</sub>/CH<sub>2</sub>F<sub>2</sub> and the fluorine atom of TIF<sub>6</sub><sup>2−</sup>.</p>
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<p>XRD patterns of TIFSIX-2-Cu-i after activation (compared to calculated patterns).</p>
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<p>Diagram of adsorption measurements’ experimental apparatus.</p>
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<p>The chemically different atoms in TIFSIX-2-Cu-i. Atom colors: C = gray; H = white; N = blue; F = green; Ti = silver; Cu = red.</p>
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11 pages, 2245 KiB  
Article
Morphology Regulation of Zeolite MWW via Classical/Nonclassical Crystallization Pathways
by Wenwen Zi, Zejing Hu, Xiangyu Jiang, Junjun Zhang, Chengzhi Guo, Konggang Qu, Shuo Tao, Dengran Tan and Fangling Liu
Molecules 2024, 29(1), 170; https://doi.org/10.3390/molecules29010170 - 27 Dec 2023
Cited by 1 | Viewed by 1388
Abstract
The morphology and porosity of zeolites have an important effect on adsorption and catalytic performance. In the work, simple inorganic salts, i.e., Na salts were used to synthesize MWW zeolite using the organic compound 1-Butyl-2,3-dimethyl-1H-imidazol-3-ium hydroxide as a structure-directing agent and the morphology [...] Read more.
The morphology and porosity of zeolites have an important effect on adsorption and catalytic performance. In the work, simple inorganic salts, i.e., Na salts were used to synthesize MWW zeolite using the organic compound 1-Butyl-2,3-dimethyl-1H-imidazol-3-ium hydroxide as a structure-directing agent and the morphology was regulated by the alkali metals. The sample synthesized without Na salts shows a dense hexagon morphology, while different morphologies like ellipsoid, wool ball, and uniform hexagon appear when using NaOH, Na2CO3, and NaHCO3, respectively. Moreover, the impact of Na salts on the induction, nucleation, and the evolution of crystal growth was studied. Different kinds of Na salts have a different impact on the crystalline induction time in the order of NaHCO3 (36 h) < Na2CO3 (72 h) = NaOH (72 h). Meanwhile, the crystalline mechanism with the cooperation of inorganic salts and the organic SDAs is proposed. NaOH- and Na2CO3-MWW zeolite crystallized with a network of hydrogel via the nonclassical pathway in the system; however, the product is synthesized via a classical route in the NaHCO3 environment. This work provides information about MWW zeolite crystallization and modulating diverse morphologies by adjusting the process. Full article
(This article belongs to the Special Issue Zeolites and Porous Materials: Synthesis, Properties and Applications)
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<p>(<b>a</b>) PXRD patterns of the synthesized MCM-22P and the calcined sample. (<b>b</b>) Rietveld refinements of MCM-22 and the structure with SDA inside. (<b>c</b>) TG thermogravimetry of the pure silica MWW zeolite synthesized with the only SDA. Experimental (red) and calculated (black) PXRD patterns as well as the positions of the Bragg reflections shown by the short tick marks (blue). (<b>d</b>) N<sub>2</sub> isotherm curve of the calcined pure silicate MCM-22.</p>
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<p>Paragraphs including the SEM, N<sub>2</sub> isotherm curves, and TEM images of MCM-22P using SDA directly and using the cooperation of SDA with NaOH, Na<sub>2</sub>CO<sub>3</sub>, and NaHCO<sub>3</sub> under the same ratio of Na<sup>+</sup>/Si = 0.1.</p>
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<p>(<b>a</b>) N<sub>2</sub> adsorption/desorption isotherms and (<b>b</b>) pore size distribution of the samples with the addition of NaHCO<sub>3</sub> under different ratios of HF/Si (a: 0.5, b: 0.65, c: 0.75, d: 1, e: 1.25).</p>
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<p>SEM pictures of the samples synthesized with Na salts at different crystalline time.</p>
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<p>Two pathways of zeolite crystallization.</p>
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<p>Crystallization pathways of MWW zeolite: NaOH/Na<sub>2</sub>CO<sub>3</sub>-added (<b>i</b>) and NaHCO<sub>3</sub>-added (<b>ii</b>).</p>
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15 pages, 2389 KiB  
Article
Simulating Crystal Structure, Acidity, Proton Distribution, and IR Spectra of Acid Zeolite HSAPO-34: A High Accuracy Study
by Xiaofang Chen and Tie Yu
Molecules 2023, 28(24), 8087; https://doi.org/10.3390/molecules28248087 - 14 Dec 2023
Cited by 48 | Viewed by 1401
Abstract
It is a challenge to characterize the acid properties of microporous materials in either experiments or theory. This study presents the crystal structure, acid site, acid strength, proton siting, and IR spectra of HSAPO-34 from the SCAN + rVV10 method. The results indicate: [...] Read more.
It is a challenge to characterize the acid properties of microporous materials in either experiments or theory. This study presents the crystal structure, acid site, acid strength, proton siting, and IR spectra of HSAPO-34 from the SCAN + rVV10 method. The results indicate: the crystal structures of various acid sites of HSAPO-34 deviate from the space group of R3¯; the acid strength inferred from the DPE value likely decreases with the proton binding sites at O(2), O(4), O(1),and O(3), contrary to the stability order in view of the internal energy; the calculated ensemble-averaged DPE is about 1525 kJ/mol at 673.15 K; and the proton siting and the proton distribution are distinctly influenced by the temperature: at low temperatures, the proton is predominantly located at O(3), while it prefers O(2) at high temperatures, and the proton at O(4) assumedly has the least distribution at 273.15–773.15 K. In line with the neutron diffraction experiment, a correction factor of 0.979 is needed to correct for the calculated hydroxyl stretching vibration (ν(O-H)) of HSAPO-34. It seems that the SCAN meta-GGA method, compensating for some drawbacks of the GGA method, could provide satisfying results regarding the acid properties of HSAPO-34. Full article
(This article belongs to the Special Issue Zeolites and Porous Materials: Synthesis, Properties and Applications)
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<p>Single silicon-doped alumino-phosphates (HSAPO-34): (<b>a</b>) the single-unit cell (1UC) with rhombohedral representation, (<b>b</b>) the expanded lattice structure. Note that the proton is omitted for simplicity.</p>
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<p>The total energy depends on the lattice volume. The proton binding sites of HSAPO-34 are (<b>a</b>) O(1), (<b>b</b>) O(2), (<b>c</b>) O(3), and (<b>d</b>) O(4).</p>
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<p>Schematic diagram for four possible Brönsted acid sites of HSAPO-34. The proton binding sites are (<b>a</b>) O1, (<b>b</b>) O2, (<b>c</b>) O3, and (<b>d</b>) O4. Noting that Al in cycn, Si in blue, P in purple, O in red, and the number in figure is the numbering of O atom.</p>
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<p>The proton distribution of HSAPO-34 depends on the temperature.</p>
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<p>Bader charges on AlO<sub>3</sub>-O(H)-SiO<sub>3</sub> fragment from four possible Brönsted acid sites of HSAPO-34. The proton binding sites are (<b>a</b>) O(1), (<b>b</b>) O(2), (<b>c</b>) O(3), and (<b>d</b>) O(4). Noting that Al in cyan, Si in blue, and O in red.</p>
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<p>Calculated ensemble-averaged DPE (&lt;DPE&gt;) of HSAPO-34 depends on the temperature.</p>
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15 pages, 10564 KiB  
Article
Efficient Selective Capture of Carbon Dioxide from Nitrogen and Methane Using a Metal-Organic Framework-Based Nanotrap
by Junjie Peng, Chengmin Fu, Jiqin Zhong, Bin Ye, Jing Xiao, Chongxiong Duan and Daofei Lv
Molecules 2023, 28(23), 7908; https://doi.org/10.3390/molecules28237908 - 2 Dec 2023
Cited by 2 | Viewed by 1668
Abstract
Selective carbon capture from exhaust gas and biogas, which mainly involves the separation of CO2/N2 and CO2/CH4 mixtures, is of paramount importance for environmental and industrial requirements. Herein, we propose an interesting metal-organic framework-based nanotrap, namely ZnAtzCO [...] Read more.
Selective carbon capture from exhaust gas and biogas, which mainly involves the separation of CO2/N2 and CO2/CH4 mixtures, is of paramount importance for environmental and industrial requirements. Herein, we propose an interesting metal-organic framework-based nanotrap, namely ZnAtzCO3 (Atz = 3-amino-1,2,4-triazolate, CO32− = carbonate), with a favorable ultramicroporous structure and electrostatic interactions that facilitate efficient capture of CO2. The structural composition and stability were verified by FTIR, TGA, and PXRD techniques. Particularly, ZnAtzCO3 demonstrated high CO2 capacity in a wide range of pressures, with values of 44.8 cm3/g at the typical CO2 fraction of the flue gas (15 kPa) and 56.0 cm3/g at the CO2 fraction of the biogas (50 kPa). Moreover, ultrahigh selectivities over CO2/N2 (15:85, v:v) and CO2/CH4 (50:50, v:v) of 3538 and 151 were achieved, respectively. Molecular simulations suggest that the carbon atom of CO2 can form strong electrostatic Cδ+···δ−O-C interactions with four oxygen atoms in the carbonate ligands, while the oxygen atom of CO2 can interact with the hydrogen atoms in the triazolate ligands through Oδ−···δ+H-C interactions, which makes ZnAtzCO3 an optimal nanotrap for CO2 fixation. Furthermore, breakthrough experiments confirmed excellent real-world separation toward CO2/N2 and CO2/CH4 mixtures on ZnAtzCO3, demonstrating its great potential for selective CO2 capture. Full article
(This article belongs to the Special Issue Zeolites and Porous Materials: Synthesis, Properties and Applications)
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<p>Selective CO<sub>2</sub> capture from N<sub>2</sub> and CH<sub>4</sub> on a nanotrap with a suitable electrostatic environment via multiple host–guest interactions. The blue dotted lines represent the electrostatic interactions between the framework and the CO<sub>2</sub> molecule.</p>
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<p>The crystal structure and pore property of ZnAtzCO<sub>3</sub>: (<b>a</b>) coordination mode, (<b>b</b>) crystal structure shown in the b-axis, and the Connolly surface in the b-axis (<b>c</b>) and a-axis (<b>d</b>) by using a spherical probe exhibiting a radius of 1 Å. The intraframework N-H···O hydrogen bonds are marked by the golden dotted lines. I and II in <a href="#molecules-28-07908-f002" class="html-fig">Figure 2</a>c represent the two types of cavities on the structure.</p>
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<p>FTIR image (<b>a</b>), PXRD patterns (<b>b</b>), TG curves (<b>c</b>), CO<sub>2</sub> adsorption–desorption isotherms at 195 K (<b>d</b>) of ZnAtzCO<sub>3</sub>.</p>
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<p>(<b>a</b>) Single-component adsorption isotherms of CO<sub>2</sub>, N<sub>2</sub> and CH<sub>4</sub> on ZnAtzCO<sub>3</sub> at 298 K. (<b>b</b>) IAST selectivity of CO<sub>2</sub>/N<sub>2</sub> (15:85, <span class="html-italic">v:v</span>) and CO<sub>2</sub>/CH<sub>4</sub> (15:85, <span class="html-italic">v:v</span>) on ZnAtzCO<sub>3</sub>.</p>
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<p>(<b>a</b>) Single-component adsorption isotherms of CO<sub>2</sub>, N<sub>2</sub>, and CH<sub>4</sub> on ZnAtzCO<sub>3</sub> at different temperatures (273 K, 288 K, and 298 K). (<b>b</b>) Isosteric heat of CO<sub>2</sub>, N<sub>2</sub>, and CH<sub>4</sub> on ZnAtzCO<sub>3</sub>.</p>
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<p>Preferential adsorption sites on the ZnAtzCO<sub>3</sub> structure for CO<sub>2</sub> (<b>a</b>), CH<sub>4</sub> (<b>b</b>), and N<sub>2</sub> (<b>c</b>) on ZnAtzCO<sub>3</sub>. The dashed line represents the host–guest interactions between the ZnAtzCO<sub>3</sub> and the gas molecules. The unit of the distance between the gas molecules and the adsorption site is Å.</p>
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<p>(<b>a</b>–<b>c</b>) The simulated adsorption density distribution of CO<sub>2</sub>, CH<sub>4</sub>, and N<sub>2</sub> on ZnAtzCO<sub>3</sub> crystal framework at 15 kPa. (<b>d</b>–<b>f</b>) The simulated adsorption density distribution of CO<sub>2</sub>, CH<sub>4</sub> and N<sub>2</sub> on ZnAtzCO<sub>3</sub> crystal framework at 100 kPa.</p>
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<p>The simulated interaction energy for CO<sub>2</sub>, CH<sub>4</sub>, and N<sub>2</sub> on ZnAtzCO<sub>3</sub>.</p>
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<p>Breakthrough curves for CO<sub>2</sub>/N<sub>2</sub> (15:85, <span class="html-italic">v:v</span>) (<b>a</b>) and CO<sub>2</sub>/CH<sub>4</sub> (50:50, <span class="html-italic">v:v</span>) (<b>b</b>) mixture on ZnAtzCO<sub>3</sub> at 298 K and 100 kPa.</p>
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10 pages, 1563 KiB  
Article
Exquisitely Constructing a Robust MOF with Dual Pore Sizes for Efficient CO2 Capture
by Yanxi Li, Yuhua Bai, Zhuozheng Wang, Qihan Gong, Mengchen Li, Yawen Bo, Hua Xu, Guiyuan Jiang and Kebin Chi
Molecules 2023, 28(17), 6276; https://doi.org/10.3390/molecules28176276 - 28 Aug 2023
Cited by 3 | Viewed by 1976
Abstract
Developing metal–organic framework (MOF) adsorbents with excellent performance and robust stability is of critical importance to reduce CO2 emissions yet challenging. Herein, a robust ultra-microporous MOF, Cu(bpfb)(bdc), with mixed ligands of N, N′-(1,4-phenylene)diisonicotinamide (bpfb), and 1,4-dicarboxybenzene (bdc) was delicately constructed. Structurally, this [...] Read more.
Developing metal–organic framework (MOF) adsorbents with excellent performance and robust stability is of critical importance to reduce CO2 emissions yet challenging. Herein, a robust ultra-microporous MOF, Cu(bpfb)(bdc), with mixed ligands of N, N′-(1,4-phenylene)diisonicotinamide (bpfb), and 1,4-dicarboxybenzene (bdc) was delicately constructed. Structurally, this material possesses double-interpenetrated frameworks formed by two staggered, independent frameworks, resulting in two types of narrow ultra-micropores of 3.4 × 5.0 and 4.2 × 12.8 Å2, respectively. The above structural properties make its highly selective separation at 273~298 K with a CO2 capacity of 71.0~86.2 mg/g. Its adsorption heat over CO2 and IAST selectivity were calculated to be 27 kJ/mol and 52.2, respectively. Remarkably, cyclic breakthrough experiments corroborate its impressive performance in CO2/N2 separation in not only dry but also 75% RH humid conditions. Molecular simulation reveals that C-H···OCO2 in the pores plays a pivotal role in the high selectivity of CO2 adsorption. These results point out the huge potential application of this material for CO2/N2 separation. Full article
(This article belongs to the Special Issue Zeolites and Porous Materials: Synthesis, Properties and Applications)
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<p>(<b>A</b>) The synthesis of PRI-1. (<b>B</b>) PXRD patterns of the simulated and as-synthesized PRI-1, as well as those after various treatments. (<b>C</b>) 195 K CO<sub>2</sub> adsorption-desorption isotherms. (<b>D</b>) TGA curve. (<b>E</b>) Comparison of thermal stabilities of PRI-1 and other MOF adsorbents. The distances are in Å.</p>
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<p>(<b>A</b>) CO<sub>2</sub> and N<sub>2</sub> adsorption isotherms of PRI-1 at 273, 283, and 298 K. (<b>B</b>) <span class="html-italic">Q</span><sub>st</sub> of CO<sub>2</sub> in PRI-1. (<b>C</b>) Comparison of CO<sub>2</sub> <span class="html-italic">Q</span><sub>st</sub> for PRI-1 with those of other top-performing MOF adsorbents. (<b>D</b>) Comparison of CO<sub>2</sub>/N<sub>2</sub> (15:85, <span class="html-italic">v</span>/<span class="html-italic">v</span>) IAST selectivity at 298 K and 1 bar and <span class="html-italic">Q</span><sub>st</sub> of CO<sub>2</sub> under ambient conditions in PRI-1 with those of reported CO<sub>2</sub>-selective MOFs.</p>
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<p>Calculated preferential binding sites for CO<sub>2</sub> (<b>A</b>) and N<sub>2</sub> (<b>B</b>) on PRI-1. The distances are in Å. Cu, C, N, O, and H atoms are shown in pink, grey, blue, red, and white, respectively.</p>
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<p>(<b>A</b>) Experimental breakthrough curves of PRI-1 for CO<sub>2</sub>/N<sub>2</sub> (15:85) binary mixture at 298 K and 1 bar. (<b>B</b>) Experimental cycling breakthrough curves of a CO<sub>2</sub>/N<sub>2</sub> (15:85) binary mixture at 298 K and 1 bar. (<b>C</b>) Experimental breakthrough for CO<sub>2</sub>/N<sub>2</sub> (15:85) under both dry and 75% RH humid conditions. C and C<sub>0</sub> stand for outlet concentration and inlet concentration of CO<sub>2</sub> and N<sub>2</sub> in the gas mixture flow, respectively.</p>
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13 pages, 6561 KiB  
Article
A Microporous Zn(bdc)(ted)0.5 with Super High Ethane Uptake for Efficient Selective Adsorption and Separation of Light Hydrocarbons
by Feng Xu, Yilu Wu, Juan Wu, Daofei Lv, Jian Yan, Xun Wang, Xin Chen, Zewei Liu and Junjie Peng
Molecules 2023, 28(16), 6000; https://doi.org/10.3390/molecules28166000 - 10 Aug 2023
Cited by 5 | Viewed by 1429
Abstract
Separating light hydrocarbons (C2H6, C3H8, and C4H10) from CH4 is challenging but important for natural gas upgrading. A microporous metal-organic framework, Zn(bdc)(ted)0.5, based on terephthalic acid (bdc) and [...] Read more.
Separating light hydrocarbons (C2H6, C3H8, and C4H10) from CH4 is challenging but important for natural gas upgrading. A microporous metal-organic framework, Zn(bdc)(ted)0.5, based on terephthalic acid (bdc) and 1,4-diazabicyclo[2.2.2]octane (ted) ligands, is synthesized and characterized through various techniques, including powder X-ray diffraction (PXRD), scanning electron microscopy (SEM), thermogravimetric analysis (TGA), and porosity analysis. The adsorption isotherms of light hydrocarbons on the material are measured and the isosteric adsorption heats of CH4, C2H6, C3H8, and C4H10 are calculated. The prediction of C2–4/C1 adsorption selectivities is accomplished using ideal adsorbed solution theory (IAST). The results indicate that the material exhibits exceptional characteristics, including a Brunauer-Emmett-Teller (BET) surface area of 1904 m2/g and a pore volume of 0.73 cm3/g. Notably, the material demonstrates remarkable C2H6 adsorption capacities (4.9 mmol/g), while CH4 uptake remains minimal at 0.4 mmol/g at 298 K and 100 kPa. These findings surpass those of most reported MOFs, highlighting the material’s outstanding performance. The isosteric adsorption heats of C2H6, C3H8, and C4H10 on the Zn(bdc)(ted)0.5 are higher than CH4, suggesting a stronger interaction between C2H6, C3H8, and C4H10 molecules and Zn(bdc)(ted)0.5. The molecular simulation reveals that Zn(bdc)(ted)0.5 prefers to adsorb hydrocarbon molecules with richer C-H bonds and larger polarizability, which results in a stronger dispersion force generated by an adsorbent-adsorbate induced polarization effect. Therefore, the selectivity of C4H10/CH4 is up to 180 at 100 kPa, C3H8/CH4 selectivity is 67, and the selectivity of C2H6/CH4 is 13, showing a great potential for separating C2–4 over methane. Full article
(This article belongs to the Special Issue Zeolites and Porous Materials: Synthesis, Properties and Applications)
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Graphical abstract

Graphical abstract
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<p>XRD patterns of the Zn(bdc)(ted)<sub>0.5</sub>·2DMF·0.2H<sub>2</sub>O (<b>top</b>) compared with the simulated pattern (<b>bottom</b>).</p>
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<p>SBU unit of Zn(bdc)(ted)<sub>0.5</sub>, where green represents Zn, gray represents C, red represents O, and blue represents N.</p>
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<p>SEM image of the Zn(bdc)(ted)<sub>0.5</sub>·2DMF·0.2H<sub>2</sub>O.</p>
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<p>Thermogravimetric analysis of the Zn(bdc)(ted)<sub>0.5</sub>·2DMF·0.2H<sub>2</sub>O.</p>
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<p>Nitrogen sorption isotherms at 77 K of the Zn(bdc)(ted)<sub>0.5</sub>, where the hollow square represents adsorption, and solid square represents desorption. The inset displays the pore size distribution curve that corresponds to it.</p>
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<p>CH<sub>4</sub> (purple olive), C<sub>2</sub>H<sub>6</sub> (blue triangle), C<sub>3</sub>H<sub>8</sub> (red circle), and C<sub>4</sub>H<sub>10</sub> (black square) sorption isotherms of Zn(bdc)(ted)<sub>0.5</sub> at (<b>a</b>) 288 K, and (<b>b</b>) 298 K.</p>
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<p>Adsorption isotherms of CH<sub>4</sub> (<b>a</b>), C<sub>2</sub>H<sub>6</sub> (<b>b</b>), C<sub>3</sub>H<sub>8</sub> (<b>c</b>), and C<sub>4</sub>H<sub>10</sub> (<b>d</b>) on the Zn(bdc)(ted)<sub>0.5</sub> at 288–308 K.</p>
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<p>The isosteric adsorption heats of CH<sub>4</sub>, C<sub>2</sub>H<sub>6</sub>, C<sub>3</sub>H<sub>8</sub>, and C<sub>4</sub>H<sub>10</sub> on Zn(bdc)(ted)<sub>0.5</sub> (black square for C<sub>4</sub>H<sub>10</sub>, red circle for C<sub>3</sub>H<sub>8</sub>, blue triangle for C<sub>2</sub>H<sub>6</sub>, and purple olive for CH<sub>4</sub>).</p>
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<p>Experimental and fitted isotherms for CH<sub>4</sub>, C<sub>2</sub>H<sub>6</sub>, C<sub>3</sub>H<sub>8</sub>, and C<sub>4</sub>H<sub>10</sub> at 298 K (black square for C<sub>4</sub>H<sub>10</sub>, red circle for C<sub>3</sub>H<sub>8</sub>, blue triangle for C<sub>2</sub>H<sub>6</sub>, and purple olive for CH<sub>4</sub>).</p>
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<p>IAST-predicted equimolar gas mixture adsorption selectivities for Zn(bdc)(ted)<sub>0.5</sub> at 298 K (black square for C<sub>4</sub>H<sub>10</sub>/CH<sub>4</sub>, red circle for C<sub>3</sub>H<sub>8</sub>/CH<sub>4</sub>, and blue triangle for C<sub>2</sub>H<sub>6</sub>/CH<sub>4</sub>).</p>
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<p>The calculated preferential adsorption site for a single (<b>a</b>) CH<sub>4</sub>, (<b>b</b>) C<sub>2</sub>H<sub>6</sub>, (<b>c</b>) C<sub>3</sub>H<sub>8</sub> and (<b>d</b>) C<sub>4</sub>H<sub>10</sub> in Zn(bdc)(ted)<sub>0.5</sub>.</p>
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<p>Interaction energy histogram for C1−C4 with Zn(bdc)(ted)<sub>0.5</sub>.</p>
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Review

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24 pages, 1989 KiB  
Review
Zeolite and Neurodegenerative Diseases
by Stefan Panaiotov, Lyubka Tancheva, Reni Kalfin and Polina Petkova-Kirova
Molecules 2024, 29(11), 2614; https://doi.org/10.3390/molecules29112614 - 2 Jun 2024
Cited by 1 | Viewed by 5798
Abstract
Neurodegenerative diseases (NDs), characterized by progressive degeneration and death of neurons, are strongly related to aging, and the number of people with NDs will continue to rise. Alzheimer’s disease (AD) and Parkinson’s disease (PD) are the most common NDs, and the current treatments [...] Read more.
Neurodegenerative diseases (NDs), characterized by progressive degeneration and death of neurons, are strongly related to aging, and the number of people with NDs will continue to rise. Alzheimer’s disease (AD) and Parkinson’s disease (PD) are the most common NDs, and the current treatments offer no cure. A growing body of research shows that AD and especially PD are intricately related to intestinal health and the gut microbiome and that both diseases can spread retrogradely from the gut to the brain. Zeolites are a large family of minerals built by [SiO4]4− and [AlO4]5− tetrahedrons joined by shared oxygen atoms and forming a three-dimensional microporous structure holding water molecules and ions. The most widespread and used zeolite is clinoptilolite, and additionally, mechanically activated clinoptilolites offer further improved beneficial effects. The current review describes and discusses the numerous positive effects of clinoptilolite and its forms on gut health and the gut microbiome, as well as their detoxifying, antioxidative, immunostimulatory, and anti-inflammatory effects, relevant to the treatment of NDs and especially AD and PD. The direct effects of clinoptilolite and its activated forms on AD pathology in vitro and in vivo are also reviewed, as well as the use of zeolites as biosensors and delivery systems related to PD. Full article
(This article belongs to the Special Issue Zeolites and Porous Materials: Synthesis, Properties and Applications)
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Figure 1

Figure 1
<p>Structure of zeolites. (<b>A</b>) Primary and secondary building units of zeolite. The primary building units represent tetrahedral structures with mostly Si or Al in the center of the tetrahedron and O atoms at the corners (left), which are shown to be linking the tetrahedrons in the secondary units (right). (<b>B</b>) Secondary building units further linked by O atoms and forming a complex three-dimensional lattice underlying the microporous structure of zeolite holding cavities filled with water molecules and ions (by Derbe et al. [<a href="#B52-molecules-29-02614" class="html-bibr">52</a>]). (<b>C</b>) Clinoptilolites from the region of Kardzhali, Rhodope mountain, South Bulgaria (collection of the Museum “Earth and People”, Sofia, Bulgaria).</p>
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<p>Overview on the various effects of zeolite in relation to neurodegenerative diseases and especially AD and PD. Green arrows denote positive effects and red arrows-negative. ND—neurodegenerative diseases, DAO—diamine oxidase, ZO-1—Zonula occludens-1.</p>
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25 pages, 1335 KiB  
Review
Zeolite Properties, Methods of Synthesis, and Selected Applications
by Natalia Kordala and Mirosław Wyszkowski
Molecules 2024, 29(5), 1069; https://doi.org/10.3390/molecules29051069 - 29 Feb 2024
Cited by 23 | Viewed by 11891
Abstract
Zeolites, a group of minerals with unique properties, have been known for more than 250 years. However, it was the development of methods for hydrothermal synthesis of zeolites and their large-scale industrial applications (oil processing, agriculture, production of detergents and building materials, water [...] Read more.
Zeolites, a group of minerals with unique properties, have been known for more than 250 years. However, it was the development of methods for hydrothermal synthesis of zeolites and their large-scale industrial applications (oil processing, agriculture, production of detergents and building materials, water treatment processes, etc.) that made them one of the most important materials of the 20th century, with great practical and research significance. The orderly, homogeneous crystalline and porous structure of zeolites, their susceptibility to various modifications, and their useful physicochemical properties contribute to the continuous expansion of their practical applications in both large-volume processes (ion exchange, adsorption, separation of mixture components, catalysis) and specialized ones (sensors). The following review of the knowledge available in the literature on zeolites aims to present the most important information on the properties, synthesis methods, and selected applications of this group of aluminosilicates. Special attention is given to the use of zeolites in agriculture and environmental protection. Full article
(This article belongs to the Special Issue Zeolites and Porous Materials: Synthesis, Properties and Applications)
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Figure 1

Figure 1
<p>Scheme of silicon and aluminum tetrahedra in the zeolite structure (own elaboration based on Khaleque et al. [<a href="#B9-molecules-29-01069" class="html-bibr">9</a>]).</p>
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<p>Elemental cell and channel system of FAU, LTA, and MFI zeolites (from Database of Zeolite Structures, International Zeolite Association [<a href="#B10-molecules-29-01069" class="html-bibr">10</a>]).</p>
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<p>Changes in the physicochemical properties of zeolites as a function of the molar ratio of silicon to aluminum (own elaboration based on Payra, Dutta [<a href="#B24-molecules-29-01069" class="html-bibr">24</a>]; Jakubowski et al. [<a href="#B31-molecules-29-01069" class="html-bibr">31</a>]).</p>
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<p>Examples of zeolite applications in industry (own elaboration based on Rhodes [<a href="#B80-molecules-29-01069" class="html-bibr">80</a>]).</p>
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