Method of preparing zeolite nanosheet via simple calcination process and zeolite nanosheet particle prepared thereby
10981797 ยท 2021-04-20
Assignee
Inventors
Cpc classification
B01J20/3078
PERFORMING OPERATIONS; TRANSPORTING
B01J20/183
PERFORMING OPERATIONS; TRANSPORTING
B01J29/7038
PERFORMING OPERATIONS; TRANSPORTING
B01J20/305
PERFORMING OPERATIONS; TRANSPORTING
C01B39/48
CHEMISTRY; METALLURGY
C01B3/56
CHEMISTRY; METALLURGY
C01P2004/24
CHEMISTRY; METALLURGY
International classification
C01B39/48
CHEMISTRY; METALLURGY
B01J20/18
PERFORMING OPERATIONS; TRANSPORTING
B01J35/00
PERFORMING OPERATIONS; TRANSPORTING
C01B3/56
CHEMISTRY; METALLURGY
C01B39/02
CHEMISTRY; METALLURGY
B01J20/30
PERFORMING OPERATIONS; TRANSPORTING
Abstract
Disclosed are a method of preparing a zeolite nanosheet and a zeolite nanosheet particle prepared thereby, and more particularly a method of preparing a zeolite nanosheet capable of preparing a monolayer zeolite nanosheet through a simple process of mixing a multilayer zeolite precursor with a swelling agent to swell the multilayer zeolite precursor and drying and calcining the multilayer zeolite precursor, wherein the monolayer zeolite nanosheet is useful to separate a catalyst or gas, and a zeolite nanosheet particle prepared thereby.
Claims
1. A method of preparing a monolayer zeolite nanosheet comprising: mixing a multilayer MWW type zeolite precursor with water and a swelling agent to swell intra-layers of the multilayer zeolite precursor; recovering a solid material from the mixture containing a swollen zeolite precursor, and then calcining the solid material to obtain a monolayer zeolite nanosheet; and drying at a temperature of 50 to 110 C. for 10 to 24 hours after the recovering the solid material, wherein the swelling agent is a mixture of a salt compound having a functional group of alkyltrimethylammonium and a salt compound having a functional group of tetrapropylammonium, and wherein an Si/AI ratio of the multilayer MWW type zeolite precursor is 10 to 200.
2. The method of preparing a monolayer zeolite nanosheet of claim 1, wherein the salt compound having the functional group of alkyltrimethylammonium is one or more selected from the group consisting of dodecyltrimethylammonium bromide, cetrimonium bromide and trimethyloctadecylammonium bromide.
3. The method of preparing a monolayer zeolite nanosheet of claim 1, wherein the salt compound having the functional group of tetrapropylammonium is one or more selected from the group consisting of tetrapropylammonium bromide, tetrapropylammonium fluoride, tetrapropylammonium chloride and tetrapropylammonium hydroxide.
4. The method of preparing a monolayer zeolite nanosheet of claim 1, wherein the mixing is performed at a temperature of 25 to 80 C. for 16 to 20 hours.
5. The method of preparing a monolayer zeolite nanosheet of claim 1, wherein the calcining is performed at a temperature of 400 to 700 C. for 1 to 40 hours.
6. The method of preparing a monolayer zeolite nanosheet of claim 1, wherein the multilayer MWW type zeolite precursor is prepared by adding an organic structure-directing agent.
7. The method of preparing a monolayer zeolite nanosheet of claim 1, wherein a half-width at half-maximum (HWHM) of a (101) plane of the monolayer zeolite nanosheet shows linear behavior with respect to a reciprocal of a number of unit cell nanosheets of the zeolite in a c-direction.
8. The method of preparing a monolayer zeolite nanosheet of claim 1, wherein a ratio of a micropore volume of the monolayer zeolite nanosheet shows linear behavior with respect to a reciprocal of a number of unit cell nanosheets of the zeolite in a c-direction.
9. A monolayer zeolite nanosheet prepared by the method according to claim 1, wherein particles having about one or two unit cell thickness, are aggregated into the monolayer zeolite nanosheet having about three to four unit cell thickness along c-axis.
10. A catalyst comprising the monolayer zeolite nanosheet of claim 9.
11. A method of separating H.sub.2 comprising contacting the monolayer zeolite nanosheet of claim 9 with a mixture containing H.sub.2 to separate H.sub.2 from the mixture.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The patent or application file contains at least one drawing executed in color. Copies of this patent or patent application publication with color drawing(s) will be provided by the Office upon request and payment of the necessary fee.
(2) The above and other objects, features and other advantages of the present invention will be more clearly understood from the following detailed description taken in conjunction with the accompanying drawings, in which:
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DETAILED DESCRIPTION OF THE INVENTION
(23) Unless defined otherwise, all technical and scientific terms used herein have the same meanings as appreciated by those skilled in the field to which the present invention pertains. In general, the nomenclature used herein is well-known in the art and is ordinarily used.
(24) In the present invention, it was found that a monolayer zeolite nanosheet can be prepared through a simple process of mixing a multilayer zeolite precursor with a swelling agent to swell the multilayer zeolite precursor and drying and calcining the multilayer zeolite precursor.
(25) Thus, in one aspect, the present invention relates to a method of preparing a monolayer zeolite nanosheet comprising: (a) mixing a multilayer zeolite precursor with water and a swelling agent to swell intra-layers of the multilayer zeolite precursor; and (b) recovering a solid material from the mixture containing a swollen zeolite precursor, and then calcining the solid material to obtain a monolayer zeolite nanosheet.
(26) In the present invention, it was found that effective delamination is possible through inter-layer swelling and calcination at room temperature, and a simple method of exfoliating layered MCM-22(P) into a few UC nanosheets (UC indicating a nanosheet of an MWW zeolite in c-direction) is provided. In particular, the structural and textural properties of hierarchically structured particles were rigorously investigated, along with the simulated porous structure. The present inventors have focused on the determination of how many layers along the c-axis were present in the resulting particles. In addition, the results of the selective titration of acid sites using two types of probes (one that can enter the 10-MR pores and one that is only accessible to the external area) were consistent with the textural properties.
(27) A layered precursor of MCM-22 (MCM-22(P)), a representative MWW type zeolite used in the present invention, is a flexible, reliable platform for structural transformation via inter-layer swelling and subsequent pillaring/delamination. In particular, the delaminated MWW type zeolite, which is a few nanometers thick, is desirable for overcoming diffusion limits. In addition, 12 membered-ring (MR) pores, which are otherwise difficult to access because of the small 10 MR pores between the 12 MR pores, are exposed in the delaminated MCM-22 configuration. Despite the promise thereof, the conventional procedure to acquire the delaminated MCM-22 is complicated. The present invention provides a simple, effective method of exfoliating MCM-22(P) into nanosheets. Calcination of swollen MCM-22(P) was found to result in successful delamination. A rigorous analysis of the structural and textural properties of the resulting delaminated layers revealed that a majority of the nanosheets had a 3 to 4 unit cell thickness along the c-axis, which were further formed via aggregation of particles having about 1 to 2 unit cell thickness. In addition, the resulting monolayer structure particles retained the original MCM-22 zeolite structure, further demonstrating the usefulness of the method according to the present invention.
(28) According to an embodiment of the present invention, a multilayer zeolite precursor is mixed with water and a swelling agent to swell the multilayer zeolite precursor, the mixture containing the swollen zeolite precursor is centrifuged to recover a solid material, and the solid material is dried and calcined to recover a monolayer zeolite nanosheet.
(29) In the present invention, the Si/Al ratio of the zeolite precursor may be 10 to 200.
(30) The swelling agent, which is a material that functions to swell the multilayer zeolite precursor, may be a mixture of a salt compound containing a functional group of alkyltrimethylammonium (CH.sub.3(CH.sub.2)N(CH.sub.3).sub.3, n=11, 15, or 17) and a salt compound containing a functional group of tetrapropylammonium ((C.sub.3H.sub.7).sub.4N)).
(31) In the present invention, preferably, the salt compound having the functional group of alkyltrimethylammonium may be one or more selected from the group consisting of dodecyltrimethylammonium bromide (C12TAB) of Chemical Formula 1, cetrimonium bromide (C16TAB or CTAB) of Chemical Formula 2, and trimethyloctadecylammonium bromide (C18TAB) of Chemical Formula 3.
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(33) In the present invention, the salt compound having the functional group of tetrapropylammonium ((C.sub.3H.sub.7).sub.4N)) may be one or more selected from the group consisting of tetrapropylammonium bromide (TPABr), tetrapropylammonium fluoride (TBAF), and tetrapropylammonium chloride (TPACl) of Chemical Formula 4 and tetrapropylammonium hydroxide (TPAOH) of Chemical Formula 5.
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(35) More preferably, the above salt compound may be a mixture of cetrimonium bromide (CTAB) and tetrapropylammonium hydroxide (TPAOH).
(36) In the present invention, mixing may be performed at a temperature of 25 to 80 C. for 16 to 20 hours. In the case in which mixing is performed within the above temperature and time ranges, the swelling effect is achieved.
(37) In the present invention, drying may be performed at a temperature of 50 to 110 C. for 10 to 24 hours.
(38) In the present invention, calcination may be performed at a temperature of 400 to 700 C. for 1 to 40 hours. In the case in which calcination is performed within the above temperature and time ranges, the swelling agent is removed, and therefore the zeolite nanosheet preparation effect is achieved.
(39) In the present invention, the multilayer zeolite precursor may be prepared by adding an organic structure-directing agent. The organic structure-directing agent may be one or more selected from the group consisting of HMI (hexamethyleneimine), piperidine, TMAdaOH (N,N,N-trimethyl adamantylammonium hydroxide), TMAdaBr (N,N,N-trimethyl adamantylammonium bromide), TMAdaF (N,N,N-trimethyl adamantylammonium fluoride), TMAdaCl (N,N,N-trimethyl adamantylammonium chloride), and TMAdaI (N,N,N-trimethyl adamantylammonium iodide).
(40) In the present invention, the corresponding half-width at half-maximum (HWHM) of a (101) plane of the monolayer zeolite nanosheet shows linear behavior with respect to the reciprocal of the number of nanosheets of the zeolite in the c-direction, or the ratio of the micropore volume of the zeolite shows linear behavior with respect to the reciprocal of the number of nanosheets of the zeolite in the c-direction.
(41) In the present invention, it has been found that a monolayer zeolite nanosheet prepared by the above method is used as a commercial catalyst in an alkylation process, accessibility to products is improved, whereby reaction activity is increased and the lifetime of the catalyst is also increased. Also, it has been found that the monolayer zeolite has a structural characteristic in that a c-direction layer is separated, and a separation membrane having high permeability can be synthesized.
(42) Thus, in another aspect, the present invention relates to a monolayer zeolite nanosheet prepared by the above method, wherein nanosheets having a thickness of 2.0 to 3.0 nm of a layer, are aggregated into one or two layers in a c-direction to compose of three to four layers having a thickness of 2.0 to 14 nm.
(43) In yet another aspect, the present invention relates to a catalyst including the monolayer zeolite nanosheet.
(44) In a further aspect, the present invention relates to an H.sub.2 separation method of bringing the monolayer zeolite nanosheet into contact with a mixture containing H.sub.2 to separate H.sub.2 from the mixture.
(45) The monolayer zeolite nanosheet according to the present invention is used not only for a catalyst but also for separation, collection, or removal of gas including H.sub.2.
(46) A monolayer zeolite nanosheet according to an embodiment of the present invention has a well-preserved MWW type structure consisting of 3 to 4 UC nanosheets formed via aggregation of about 1 to 2 UC nanosheets in the c-direction. In particular, rigorous analysis of the structural (XRD) and textural (Ar adsorption) features, along with a selective acid site titration method and NMR spectra, reveals that RT_NS consisted of a well-preserved MWW type zeolite structure with a large number of total Brnsted acid sites. Because RT_NS has high potential as a unique catalyst, RT_NS can be applied to catalytic reactions (starting with methanol-to-hydrocarbon catalysis).
(47) Hereinafter, the present invention will be described in more detail with reference to examples. However, it will be obvious to those skilled in the art that these examples are provided only for illustration of the present invention and should not be construed as limiting the scope of the present invention.
Example
Preparation Example 1: Preparation of MCM-22(P) Monolayer Zeolite Nanosheet
Preparation Example 1-1: Synthesis of MCM-22(P) Particles
(48) MCM-22(P) particles were synthesized according to the reported method (Corma, A. et al. J., Zeolites, 1995, 15, 2-8). In detail, 0.59 g of sodium aluminate (about 55% Al.sub.2O.sub.3 and 45% Na.sub.2O, Sigma-Aldrich) and 2.0 g of sodium hydroxide (98%, Sigma-Aldrich) were dissolved in 261.3 g of deionized water. After mixing the solution using a stirring bar, 19.9 g of fumed silica (CAB-O-SIL M5, Cabot) was added to the solution. Subsequently, 16.2 g of hexamethyleneimine (HMI, 99%, Sigma-Aldrich) was added dropwise to the mixture while stirring. The final molar composition of the mixture was 100 SiO.sub.2: 1.93 Al.sup.3+: 17.9 Nat: 49.3 HMI: 4,377 H.sub.2O. The mixture was further shaken overnight at room temperature. Subsequently, the mixture was transferred to Teflon liners and allowed to react in a Teflon lined stainless-steel autoclave at 408 K for 11 days. The resulting product was recovered by repeated centrifugation and washing with deionized water five times. The recovered product was dried at 70 C., and, for convenience, is referred to as MCM-22(P), where P inside the parentheses indicates that it is the MCM-22 precursor. A portion of the dried MCM-22(P) was calcined at 823 K for 12 hours at a ramp rate of 1 C./min under 200 mL/min of airflow in a boxed furnace. The calcined particles are denoted MCM-22(C), where C inside the parentheses indicates calcined MCM-22.
Preparation Example 1-2: Post-Treatment of MCM-22(P) Particles
(49) MCM-22(P) was post-treated for structural transformation to the delaminated form. First, MCM-22(P) was swollen at two different temperatures (RT: room temperature and HT: 80 C.) in accordance with the reported studies (Maheshwari, S. et al., J. Am. Chem. Soc., 2008, 130, 1507-1516; Schwanke, A. J. et al., Microporous Mesoporous Mater., 2017, 254, 17-27). The molar composition for the swelling step was identical to those reported in the literature (Corma, A. et al., Nature, 1998, 396, 353-356; Corma, A. et al., J. Catal., 2000, 191, 218-224; Corma, A. et al., J. Catal., 1999, 186, 57-63). Specifically, 3.4 g of cetyltrimethylammonium bromide (CTAB, 99%, Sigma-Aldrich) and 3.7 g of a tetrapropylammonium hydroxide solution (TPAOH, 40 wt %, Alfa Aesar) were added sequentially to 10.8 g of deionized water. After that, about 0.6 g of MCM-22(P) particles was added to the swelling solution. The mixture was stirred for 16 hours at two different temperatures to promote swelling. The swollen MCM-22(P) at 80 C. was further subjected to sonication and acidification. For sonication, a conical tube containing the whole mixture was placed in a bath-type sonicator (UC-10P, JEIO Tech), and the tube was sonicated for 60 min. Subsequently, a certain amount of a hydrochloric acid solution (1 M, Sigma-Aldrich) was added to the sonicated mixture until the pH value reached about 2 (usually, 1.95 to 2.05). The resulting particles were recovered through centrifugation and further dried at 70 C. The dried particles were calcined at 823 K for 12 hours at a temperature increase rate of 1 C./min under 200 mL/min of airflow in a boxed furnace (CRF-M30-UP, Pluskolab). The resulting calcined particles are denoted HT_S_H, where HT indicates the high swelling temperature, S indicates bath type sonication, and H indicates acid addition, respectively. In addition, the swollen MCM-22(P) particles at room temperature were recovered through the above-mentioned procedure, but without sonication or pH adjustment. After the same calcination process, the resulting particles are referred to as RT_NS, where RT indicates room-temperature swelling and NS represents no sonication.
Example 1: Simulation Model and Characterization
(50) Scanning electron microscopy (SEM) images were obtained using a field emission scanning electron microscope (FE-SEM) (Hitachi S-4300). A Pt coating was applied to all samples via ion sputtering (Hitachi E-1030) to obtain SEM images. X-ray diffraction (XRD) patterns were acquired in the /2 configuration using a Rigaku Model D/Max-2500V/PC diffractometer with Cu K radiation (40 kV, 100 mA, =0.154 nm). Transmission electron microscopy (TEM) images were acquired using a field-emission transmission electron microscope (FE-TEM) (Tecnai G.sup.2 F30ST). N.sub.2 physisorption data at 77 K and Ar physisorption data at 87 K were acquired using the same instrument (ASAP 2020, Micromeritics, Inc.). Before measurement, the samples were degassed at about 350 C. in a vacuum for at least 12 hours. .sup.29Si magic angle spinning nuclear magnetic resonance (MAS NMR) spectra were obtained using an AVANCE III HD 400 (Bruker) NMR spectrometer with a magnetic field of 9.4 T. Each spectrum was recorded 2,700 times at 79.4 MHz with a spinning rate of 6 kHz for .sup.29Si MAS NMR, whereas that for .sup.27Al MAS NMR was recorded 1,024 times at 104.2 MHz with a spinning rate of 10 kHz. 4,4-Dimethyl-4-silapentane sulfonate sodium (DSS) and Al(NO.sub.3).sub.3 were used as references for the .sup.29Si and .sup.27Al MAS NMR spectra, respectively. The temperature-programmed desorption of NH.sub.3 (referred to as NH.sub.3-TPD-MS) was conducted with a BEL-CAT (MicrotracBEL Corp.) and monitored with a BELMass (MicrotracBEL Corp.). After the activation of a sample at 500 C. for 1 hour under the flow of He and cooling to room temperature, the sample was further allowed to adsorb NH.sub.3 molecules for 30 minutes under the flow of 5 vol % NH.sub.3 gas, with the balance of He, at 30 mL/min. Subsequently, the sample was gradually heated up to 800 C. at a ramp rate of 10 C./min under the flow of He at 30 mL/min. The effluent NH.sub.3 from the sample was monitored by mass spectrometry (BELMass). In-situ pyridine adsorption was carried out in a custom-made cell, where ZnSe windows were used for the windows on both sides. Before measurement, the sample was activated at 500 C. for 6 hours at a ramp rate of 3 C./min in a vacuum. After completing the activation process, the reference IR spectra were obtained at 150 C., and subsequently, pyridine vapor (Py) was added, and the sample was left for adsorption for 1 hour; for the Py vapor (partial vapor pressure of 2.08 kPa at 298 K), He was made to flow at 30 mL/min through a Py-containing bubbler. The weakly and physically adsorbed pyridine vapor was removed by applying a vacuum for 1 hour at 150 C. Subsequently, the IR spectra of the Py-adsorbed sample (denoted Py-spectra) were recorded. To examine the Brnsted acid sites in the non-microporous area (i.e., mesoporous and external surface areas), adsorption experiments with a bulkier pyridine derivative (here, 2,6-di-tertbutylpyridine; dTBPy, partial vapor pressure of 0.034 kPa at 298 K) were carried out by following the same procedure as for the pyridine adsorption experiments. The obtained spectra are labeled the dTBPy-spectra. Finally, the spectra, obtained by subtracting the reference data from the Py-spectra or dTBPy-spectra, were integrated for 1,540-45 cm.sup.1 (Py) and 1,615 cm.sup.1 (dTBPy) to quantify the total Brnsted acid sites and the Brnsted acid sites on the mesoporous and external surface areas, respectively. The extinct coefficients corresponding to wavenumbers of 1,540-45 and 1,615 cm.sup.1 were 1.13 (Meloni, D. et al., Appl. Catal. A-Gen., 2001, 215, 55-66) and 5.3 cm.Math.mol.sup.1 (Gora-Marek, K. et al., J. Phys. Chem. C, 2014, 118, 12266-12274), respectively.
(51) To investigate the Ar adsorption behavior in the delaminated MWW type zeolite, Ar adsorption isotherms were computed using grand-canonical Monte Carlo (GCMC) simulations at 88 K. Specifically, the GCMC simulations were carried out with 50,000 initializations and 150,000 equilibrium cycles at each pressure ranging from 10.sup.5 Pa to 90,000 Pa. The structure of the bulk MWW type zeolite was downloaded from the International Zeolite Association (IZA, http://www.iza-structure.org/databases/), and the original bulk MWW type zeolite structure was modified. In detail, for bulk MWW type zeolite, a 111 unit cell was repeated in periodic boundary conditions, whereas 111 and 112 unit cells with certain distances between the adjacent unit cells along the c-axis were used to describe 1 and 2 unit cells of the MWW type zeolite, respectively. Specifically, unit cell separations of 2, 4, and 10 nm pores were tested. In addition, the surface of the MWW type zeolite was terminated with the (100) surface by cleaving the zeolite in Materials Studio, and the dangling atoms were capped with hydrogen (refer to
(52) Elucidation of the Delaminated Structure Based on X-Ray Analysis
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(54) TABLE-US-00001 TABLE 1 Si/Al ratio estimated from measurement of SEM-EDX of MCM-22(C), HT_S_H, and RT_NS. Sample Si/Al ratio.sup.a MCM-22(C) 50.7 6.7 HT_S_H 37.4 6.1 RT_NS 34.2 4.8 .sup.aEDX data were obtained by averaging data obtained from 6 particles and calculating the standard deviation value thereof.
(55) Compared to MCM-22(C), both HT_S_H and RT_NS had some features in common; (1) broader XRD patterns, (2) decreased XRD intensities, and (3) lower signal-to-noise (S/N) ratios. These features indicate that the original MCM-22(P) particles became smaller or suffered from structural damage/collapse after the post-treatment processes (Corma, A. et al., Nature, 1998, 396, 353-356; Corma, A. et al., J. Catal., 1999, 186, 57-63; Frontera, P. et al., Microporous Mesoporous Mater., 2007, 106, 107-114). The morphological changes of HT_S_H and RT_NS compared to MCM-22(C) (
(56) To investigate the structure of HT_S_H and RT_NS in a rigorous way, the simulated XRD patterns shown in
Example 2: Elucidation of the Delaminated Structure Based on Textural Properties
(57) Along with the bulk-scale structural information from XRD analyses, the Ar adsorption isotherms of all three particles were measured to understand the textural properties thereof at the bulk scale (
(58) TABLE-US-00002 TABLE 2 Textural properties of MCM-22(C), HT_S_H, and RT_NS obtained from analysis of Ar physisorption isotherms thereof. V.sub.micro.sup.b S.sub.ex S.sub.micro (cm.sup.3 .Math. g.sup.1) V.sub.micro (%, vs. S.sub.meso (%, vs. H-K (%, vs. Si/Al S.sub.BET S.sub.ex.sup.b MCM- (m.sup.2 .Math. g.sup.1) S.sub.micro.sup.b MCM- 10 MR + MCM- Adsorbate Sample ratio.sup.a (m.sup.2 .Math. g.sup.1) (m.sup.2 .Math. g.sup.1) 22) t-plot.sup.b BJH.sup.c (m.sup.2 .Math.g.sup.1) 22) t-plot 12 MR 22).sup.d N.sub.2 MCM-22(C) 50 576 82 100 494 100 0.18 100 (50.7) HT_S_H 50 880 398 485 371 534 110 22 0.02 11 (37.4) RT_NS 50 579 278 339 35 80 266 54 0.11 61 (34.2) Ar MCM-22(C) 50 500.1 149.6 100 350.5 100 0.17 0.116 100 (50.7) HT_S_H 50 818.5 329.2 220 633 489.3 140 0.02 0.001 0.9 (37.4) RT_NS 50 510.2 276.2 185 124 234.0 67 0.07 0.062 53 (34.2) Notation: S.sub.BET, Brunauer-Emmett-Teller (BET) surface area; S.sub.ex, external surface area; S.sub.meso, mesoporous surface area; S.sub.micro, microporous surface area; V.sub.micro, micropore volume; V.sub.total, total pore volume; V.sub.meso, mesopore volume; , not available .sup.aobtained from nominal values and actual values in parenthesis. .sup.bcalculated using a modified t-plot method and the conventional t-plot method for N.sub.2 and Ar adsorption isotherms, respectively. Of these two, the results based on the former method are more reliable and adopted for comparison in the present invention. .sup.ccalculated using the BJH method in the range of 2-50 nm. .sup.dobtained by calculating the numerical values obtained via the t-plot method for N.sub.2 adsorption isotherms and the H-K method for Ar adsorption isotherms.
(59) In addition, the isotherm of HT_S_H shown in
(60) TABLE-US-00003 TABLE 3 Textural properties of MCM-22(C), HT_S_H, and RT_NS obtained from N.sub.2 physisorption isotherms thereof. S.sub.BET S.sub.ex.sup.b S.sub.ex S.sub.meso S.sub.micro.sup.d S.sub.micro V.sub.total.sup.e V.sub.micro.sup.b V.sub.micro V.sub.meso.sup.b Si/Al (m.sup.2 .Math. (m.sup.2 .Math. (%,vs. (m.sup.2 .Math.g.sup.1) (m.sup.2 .Math. (%, vs. (cm.sup.3 .Math. (cm.sup.3 .Math. (% vs. (cm.sup.3 .Math. Reference Sample ratio.sup.a g.sup.1) g.sup.1) MCM-22 t-plot.sup.b BJH.sup.c g.sup.1) MCM-22) g.sup.1) g.sup.1) MCM-22) g.sup.1) literature MCM-22(C) 50 576 82 100 494 100 0.53 0.18 100 Present (50.7) invention HT_S_H 50 880 398 485 371 534 110 22 1.22 0.02 11 0.65 Present (37.4) invention RT_NS 50 579 278 339 35 80 266 54 0.55 0.11 61 0.17 Present (34.2) invention MCM-22 .sup.50(-) 398 0.14 Corma et al. ITQ-2_C .sub.50(-) 840 790 50 Corma et al. Delaminated 368 0.05 36 Varoon MWW () et al. nanosheet DS-ITQ-2 .sub.15(-) 545 304 241 2.06 0.12 71 0.41 Margarit et al. MIT-1 20 513 321 1.014 0.131 92 Luo et al. (16) Notation: S.sub.BET, Brunauer-Emmett-Teller (BET) surface area; S.sub.ex, external surface area; S.sub.meso, mesoporous surface area; S.sub.micro, microporous surface area; V.sub.micro, micropore volume; V.sub.total, total pore volume; V.sub.meso, mesopore volume; , not available .sup.aobtained from nominal values and actual values in parenthesis. .sup.bvalue obtained from the modified t-plot. .sup.cvalue calculated using the BJH method in the range of 2-50 nm. .sup.dThe microporous surface area is the value obtained by subtracting the external surface area and the mesoporous surface area from the BET surface area. .sup.evalue calculated from P/P0 0.99. *Corma, A. et al., Nature, 1998, 396, 353-356. *Varoon, K. et al., Science, 2011, 334, 72-75. *Margarit, V. J. et al., Angew. Chem.-Int. Edit., 2015, 54, 13724-13728. *Luo, H. Y. et al., Chem. Sci., 2015, 6, 6320-6324.
(61) Compared to the other two samples, RT_NS had Ar and N.sub.2 adsorption isotherms similar to those of MCM-22(C), with a minor difference being the slight increase in adsorption in the non-microporous region (
(62) TABLE-US-00004 TABLE 4 Concentration of Brnsted acid sites in proton-exchanged MCM-22(C), HT_S_H, and RT_NS measured by pyridine (Py) and 2,6-di-tert-butylpyridine (dTBPy) adsorption. External + mesoporous PyH.sup.+ dTBPyH.sup.+ dTBPyH.sup.+/ surface area/ Sample (mol/g) (mol/g) PyH.sup.+ BET surface area MCM-22(C) 270 41 0.15 0.14 HT_S_H 141 109 0.77 0.87 RT_NS 176 108 0.61 0.54
(63) The ratio of the amount of dTBPyH.sup.+ to that of PyH.sup.+ indicates the number of B acid sites on the external+mesoporous area relative to that of the total B acid sites. For comparison, the ratio of external and mesoporous surface area to the BET surface area, obtained from the N.sub.2 physisorption measurements, is included.
(64) The similarity of the microporous structures of RT_NS and DS-ITQ-2 suggests that the layers of RT_NS were likely a combination of 1 and 2 UC nanosheets (Table 3). Referring to the N.sub.2 physisorption results of many MWW derivative materials, it was also found that RT_NS showed N.sub.2 adsorption isotherm behavior comparable to those of DS-ITQ-2 and other delaminated MWW type materials (
(65) TABLE-US-00005 TABLE 5 Textural properties of MCM-22(C), HT_S_H, and RT_NS obtained from Ar physisorption isotherms thereof. S.sub.ex V.sub.micro S.sub.BET S.sub.micro+meso.sup.a S.sub.ex.sup.a (%, vs. V.sub.micro.sup.a (%, vs. V.sub.micro.sup.b Sample Adsorbate (m.sup.2 .Math. g.sup.1) (m.sup.2 .Math. g.sup.1) (m.sup.2 .Math. g.sup.1) MCM-22) (cm.sup.3 .Math. g.sup.1) MCM-22) (cm.sup.3 .Math. g.sup.1) MCM-22(C) Ar 500.1 350.5 149.6 100 0.17 100 0.17 HT_S_H Ar 818.5 489.3 329.2 220 0.02 12 0.15 RT_NS Ar 510.2 234.0 276.2 185 0.07 44 0.14 HT_S_H-2 Ar 808.7 403.7 404.0 270 0.03 17 0.16 RT_NS-2 Ar 502.9 223.8 279.1 187 0.07 41 0.12 In order to confirm the reproducibility of the delamination process, Ar physisorption isotherms of HT_S_H and RT_NS, obtained through other experiments, were further obtained. Data obtained at this time are denoted by HT_S_H-2 and RT_NS-2. Notation: S.sub.BET, BET surface area; S.sub.ex, external surface area; S.sub.micro, microporous surface area; V.sub.micro, micropore volume .sup.acalculated using the t-plot method. .sup.bcalculated using the H-K method.
(66) The simulated Ar adsorption isotherm for the bulk MWW zeolite in
Example 3: Morphological Determination of Delaminated Particles
(67) In the present embodiment, the present inventors attempted to quantify the number of UC nanosheets in the layered MWW type zeolites based on both XRD and micropore volume/area analyses (
(68) In addition, the number of UC contained within HT_S_H and RT_NS was deduced from the external surface area, as reported in the literature. Assuming that MCM-22(C) mainly included 10 UC nanosheets (equivalent to a thickness of about 25 nm along the c-axis) with a square of 1 m in the ab-plane, a comparison of the external surface areas suggests that HT_S_H and RT_NS largely included about 2 to 3 and about 3 to 4 UC nanosheets, respectively (Table 6). Thus, considering that HT_S_H had a large external surface area attributable to amorphization, HT_S_H likely included sheets thicker than 2 UC nanosheets. As mentioned above, comprehensive analyses based on the XRD results, and the surface area and volumes of RT_NS compared to those of MCM-22(C) showed that RT_NS included about 1 to 2 UC nanosheets because of the effective delamination of MCM-22(P) while maintaining high structural integrity. On the basis of the results, these 1 to 2 UC nanosheets aggregated, resulting in the about 3 to 4 UC nanosheets in RT_NS.
(69) TABLE-US-00006 TABLE 6 Theoretical and measured values of external surface area of MWW type zeolite and derivatives thereof. Relative value based on External theoretical and measured surface values of external surface Sample a(nm).sup.b b(nm).sup.b c(nm) (m.sup.2/g) area of MCM-22(C) Theoretical 1,000 1,000 25 53 1 value (10-UC nanosheets) 1,000 1,000 15 87 1.6 (6-UC nanosheets) 1,000 1,000 7.5 171 3.2 (3-UC nanosheets) 1,000 1,000 5.0 255 4.8 (2-UC nanosheets) 1,000 1,000 2.5 507 9.6 (1-UC nanosheets) MCM-22(C).sup.a N/A N/A N/A 82 1 HT_S_H.sup.a N/A N/A N/A 398 4.9 RT_NS.sup.a N/A N/A N/A 278 3.4 .sup.avalue calculated from N2 physisorption isotherm of FIG. 12(a1). .sup.bvalue estimated from shape of MCM-22(P) of FIG. 8(a). .sup.ctheoretical value of external surface area of MWW type zeolite, calculated assuming that MWW type zeolite is cuboidal.
(70) Along with the SEM images in
(71) The Brnsted acid sites (B acid sites) in the microporous and mesoporous/external surface areas in protonated form HT_S_H and RT_NS were quantified via FT-IR analysis using independent titration methods with Py and dTBPy (Table 2) and NH.sub.3-TPD (
(72) TABLE-US-00007 TABLE 7 Quantitative values of Bronsted acid sites of MCM-22(C), HT_S_H, and RT_NS obtained by pyridine (Py) and 2,6-di-tert-butylpyridine (dTBPy) adsorption. Proton- exchange process for all samples was carried out at 80 C. PyH.sup.+ dTBPyH.sup.+ Sample (mol/g) (mol/g) dTBPyH.sup.+/PyH.sup.+ MCM-22(C) 262 21 0.08 HT_S_H 124 81 0.65 RT_NS 175 70 0.40
(73) ITQ-2, whose preparation method is identical to that of HT_S_H in the present invention, showed unique and much improved catalytic performances in the form of larger molecules and longer lifetimes, apparently because of the improved structural accessibility to acid sites. Considering that the RT_NS consisted of about 3 to 4 UC nanosheets (formed via aggregation of about 1 to 2 UC nanosheets) with a well-preserved MWW type zeolite structure and had a considerable number of total Brnsted acid sites with a higher accessibility, the catalytic investigation of RT_NS is a necessary follow-up task.
Example 4: Structural Integrity of Delaminated Particles
(74) Finally, the structural integrity of the delaminated particles was investigated using .sup.29Si and .sup.27Al MAS NMR spectra (
(75) The present invention provides a simple yet reliable method of delaminating the MWW type zeolite through direct calcination of the swollen MCM_22(P) under ambient conditions. Through substantial characterization of the physicochemical properties of HT_S_H and RT_NS, the present inventors found that the HT_S_H structure collapsed and was converted to an amorphous phase, apparently caused by the severe reaction conditions (80 C. and pH of about 13.5) used for swelling. On the other hand, RT_NS showed well-preserved MWW intermediate layers or unit cells along the c-axis and consisted of bundles or stacks of such intermediate layers with approximately 3 to 4 UC nanosheets, which were formed via aggregation of about 1 to 2 UC nanosheets. In particular, rigorous analysis of the structural (XRD) and textural (Ar adsorption) features, along with the selective acid site titration method and NMR spectra, revealed that RT_NS consisted of a well-preserved MWW type zeolite structure with a large number of total Brnsted acid sites. Because RT_NS has high potential as a unique catalyst, RT_NS may be applied to catalytic reactions (starting with conventional methanol-to-hydrocarbon catalysis).
INDUSTRIAL APPLICABILITY
(76) According to the present invention, it is possible to synthesize a zeolite having a monolayer structure through a simple calcination process, rather than a conventional complicated process. The synthesized monolayer zeolite can be used as a commercial catalyst in an alkylation process. Due to the structural characteristics thereof, accessibility of the monolayer zeolite to reactants and products is improved, whereby an increase in reaction activity and an increase in the lifetime of the catalyst can be expected.
(77) In addition, a c-direction layer of the monolayer zeolite is separated, and a separation membrane having high permeability can be synthesized using the same.
(78) Although specific configurations of the present invention have been described in detail, those skilled in the art will appreciate that the above description is provided to set forth preferred embodiments for illustrative purposes and should not be construed as limiting the scope of the present invention. Therefore, the substantial scope of the present invention is defined by the accompanying claims and equivalents thereto.