INORGANIC POROUS FRAMEWORKLAYERED DOUBLE HYDROXIDE CORESHELL MATERIALS
20190092644 ยท 2019-03-28
Inventors
Cpc classification
B82Y40/00
PERFORMING OPERATIONS; TRANSPORTING
C01B37/02
CHEMISTRY; METALLURGY
B82Y30/00
PERFORMING OPERATIONS; TRANSPORTING
C01B39/46
CHEMISTRY; METALLURGY
C01P2002/72
CHEMISTRY; METALLURGY
International classification
C01B39/02
CHEMISTRY; METALLURGY
C01B39/46
CHEMISTRY; METALLURGY
C01B37/02
CHEMISTRY; METALLURGY
Abstract
Core @ layered double hydroxide shell materials of the invention have the formula:
T.sub.p@{[M.sup.z+.sub.(1x)M.sub.x.sup.y+(OH).sub.2].sup.a+(X.sup.n).sub.a/n.Math.bH.sub.2O.Math.c(AMO-solvent)}.sub.q
wherein T is a solid, porous, inorganic oxide-containing framework material, M.sup.z+ is a metal cation of charge z or a mixture of two or more metal cations each independently having the charge z; M.sup.y+ is a metal cation of charge y or a mixture of two or more metal cations each independently having the charge y; z=1 or 2; y=3 or 4; 0<x<0.9; b is 0 to 10; c is 0.01 to 10; p>0; q>0; X.sup.n is an anion; with n>0; a=z(1x)+xy2; and AMO-solvent is an organic solvent which is completely miscible with water.
Also disclosed are the products obtained by calcining the core @ layered double hydroxide shell materials which calcination products are core @ mixed metal oxide materials having the formula
T.sub.p@[{M.sup.z+.sub.1xM.sup.y+.sub.xO.sub.w].sub.p]
wherein T is a solid, porous, inorganic oxide-containing framework material, M.sup.z+.sub.1xM.sup.y+.sub.xO.sub.w is a mixed metal oxide, or mixture of mixed metal oxides, which may be crystalline or non-crystalline, wherein M.sup.z+ and M.sup.y+ are different charged metal cations; M.sup.z+ is a metal cation of charge z or a mixture of two or more metal cations each independently having the charge z; M.sup.y+ is a metal cation of charge y or a mixture of two or more metal cations each independently having the charge y; z is 1 or 2; y is 3 or 4; 0<x<0.9; w>0; p>0 and q>0; is the residue of an X.sup.n anion in which n>0.
Claims
1. A core @ layered double hydroxide shell material having the formula
T.sub.p@{[M.sup.z+.sub.(1x)M.sub.x.sup.y+(OH).sub.2].sup.a+(X.sup.n).sub.a/n.Math.bH.sub.2O.Math.c(AMO-solvent)}.sub.q wherein T is a solid, porous, inorganic oxide-containing framework material, Mz.sup.+ is a metal cation of charge z or a mixture of two or more metal cations each independently having the charge z; M.sup.y+ is a metal cation of charge y or a mixture of two or more metal cations each independently having the charge y; z=1 or 2; y=3 or 4; 0<x<0.9; b is 0 to 10; c is 0.01 to 10; p>0; q>0; X.sup.n is an anion; with n>0; a=z(1x)+xy2; and AMO-solvent is an organic solvent which is completely miscible with water.
2. A material according to claim 1, wherein T is a molecular sieve material selected from silicate, aluminium silicate, vanadium silicate, iron silicate, silicon-aluminium phosphate (SAPO) and aluminium phosphate (AIPO), preferably an aluminium silicate having a silicon:aluminium ratio of from 1 to 100, more preferably of 1 to 50, most preferably 1 to 40.
3. A material according to claim 1, wherein the aluminium silicate has a framework structure selected from zeolite types LTA, FAU, BEA, MOR and MFI and preferably the aluminium silicate has a framework structure containing non-framework organic and/or inorganic cations, more preferably the non-framework organic and inorganic cations are selected from NR4.sup.t, where R is an optionally-substituted alkyl group, Na.sup.+, K.sup.+ and Cs.sup.+.
4. A material according to claim 1, wherein the aluminium silicate is a crystalline aluminosilicate zeolite having a composition in terms of mole ratios of oxides as follows:
M.sup.n+.sub.2/nO:Al.sub.2O.sub.3:SiO.sub.2:H.sub.20 wherein M.sup.n+ is at least one cation having a valence n, =0.90.2; is at least 2 and is between 0 and 40.
5. A material according to claim 1, wherein M is Al or Fe and/or M is Li, Mg, Ca, Co, Cu, Ni, or Cr or a mixture of two or more thereof and/or X.sup.n is selected from CO.sub.3.sup.2, OH.sup., F.sup., Cl.sup., Br.sup., SO.sub.4.sup.2, NO.sub.3.sup. and PO.sub.4.sup.3, preferably from CO.sub.3.sup.2, Cl.sup. and NO.sub.3.sup., or a mixture of two or more thereof.
6. A material according to claim 1, wherein M is Mg, M is Al and X.sup.n is CO.sub.3.sup..
7. A material according to claim 1, wherein the core @ layered double hydroxide shell material has the general formula Id
T.sub.p@{[M.sup.z+.sub.(1x)M.sup.y+.sub.x(OH).sub.2].sup.a+(X.sup.n).sub.a/n.Math.bH.sub.2O.Math.c(ethanol)}.sub.q (Id) wherein, T is; i) an aluminium silicate with a framework structure selected from zeolite types LTA, FAU, BEA, MOR or MFI; ii) an aluminophosphate; iii) a silicoaluminophosphate; or iv) a mesoporous silicate, wherein the aluminium silicate has a silicon:aluminium ratio of from 1 to 50, more preferably of 1 to 40, most preferably of 1 to 30; and the aluminium silicate has a framework structure containing non-framework organic and/or inorganic cations, more preferably the non-framework organic and inorganic cations are selected from NR.sub.4.sup.+, where R is an optionally-substituted alkyl group, Na.sup., K.sup.+ and Cs.sup.+; M.sup.z+ is selected from Li.sup.+, Ca.sup.2+, Cu.sup.2+, Zn.sup.2+, Ni.sup.2+ or Mg.sup.2+, and M.sup.y+ is Al.sup.3+, Ga.sup.3+, In.sup.3+, Fe.sup.3+; 0<x<0.9; b is 0 to 10; c is 0.01 to 10; p>0, q>0; X.sup.n is is selected from CO.sub.3.sup.2 or NO.sub.3.sup.; with n>0 (preferably 1-5) a=z(1x)+xy2.
8. A method of making a core @ layered double hydroxide shell material according to claim 1, having the formula
T.sub.p@{[M.sup.z+.sub.(1x)M.sub.x.sup.y+(OH).sub.2].sup.a+(X.sup.n).sub.a/n.Math.bH.sub.2O.Math.c(AMO-solvent)}.sub.q wherein T is a solid, porous, inorganic oxide-containing framework material, M.sup.z+ is a metal cation of charge z or a mixture of two or more metal cations each independently having the charge z; M.sup.y+ is a metal cation of charge y or a mixture of two or more metal cations each independently having the charge y; z=1 or 2; y=3 or 4; 0<x<0.9; b is 0 to 10; c is 0.01 to 10; p>0; q>0; X.sup.n is an anion; with n>0; a=z(1x)+xy2; and AMO-solvent is an organic solvent which is completely miscible with water; which method comprises the steps: (a) contacting a metal ion-containing solution containing metal ions M.sup.z+ and M.sup.y+ and particles of the framework material in the presence of a base and an anion solution; and (b) optionally treating the product with AMO-solvent and recovering the solvent treated material to obtain the core @ layered double hydroxide material.
9. A method according to claim 8, wherein T is a molecular sieve material selected from silicate, aluminium silicate, vanadium silicate, iron silicate, silicon-aluminium phosphate (SAPO) and aluminium phosphate (AIPO).
10. A method according to claim 8, wherein T is a molecular sieve material which is an aluminium silicate having a silicon:aluminium ratio of from 1 to 100, preferably 1 to 50, more preferably 1 to 40.
11. A method according to claim 8, wherein the aluminium silicate is a crystalline aluminosilicate zeolite having a composition in terms of mole ratios of oxides as follows:
M.sup.n+.sub.2/nO:Al.sub.2O.sub.3:SiO.sub.2:H.sub.20 wherein M.sup.n+ is at least one cation having a valence n, =0.90.2; is at least 2 and is between 0 and 40.
12. A core @ mixed metal oxide material having the formula
T.sub.p@{[M.sup.z+.sub.1xM.sup.y+.sub.xO.sub.w].sub.p] wherein T is a solid, porous, inorganic oxide-containing framework material, M.sup.z+.sub.1xM.sup.y+.sub.xO.sub.w is a mixed metal oxide, or mixture of mixed metal oxides, which may be crystalline or non-crystalline, wherein M.sup.z+ and M.sup.y+ are different charged metal cations; M.sup.z+ is a metal cation of charge z or a mixture of two or more metal cations each independently having the charge z; M.sup.y+ is a metal cation of charge y or a mixture of two or more metal cations each independently having the charge y; z is 1 or 2; y is 3 or 4; 0<x<0.9; w>0; p>0 and q>0; is the residue of an X.sup.n anion in which n>0.
13. A method of making a core @ mixed metal oxide according to claim 12, which method comprises subjecting a core @ layered double hydroxide shell material having the formula
T.sub.p@{[M.sup.z+.sub.(1x)M.sub.x.sup.y+(OH).sub.2].sup.a+(X.sup.n).sub.a/n.Math.bH.sub.2O.Math.c(AMO-solvent)}.sub.q wherein T is a solid, porous, inorganic oxide-containing framework material, to heat treatment wherein M.sup.z+ is a metal cation of charge z or a mixture of two or more metal cations each independently having the charge z; M.sup.y+ is a metal cation of charge y or a mixture of two or more metal cations each independently having the charge y; z=1 or 2; y=3 or 4; 0<x<0.9; b is 0 to 10; c is 0.01 to 10; p>0; q>0; X.sup.n is an anion; with n>0; a=z(1x)+xy2; and AMO-solvent is an organic solvent which is completely miscible with water.
14. A method according to claim 13, wherein the core @ layered double hydroxide shell material is subjected to heat treatment at a temperature of from 100 to 1000 C., preferably from 400 to 550 C.
15. A method according to claim 13, wherein the heat treatment is carried out in specific atmosphere, preferably in air or a nitrogen atmosphere or hydrogen atmosphere.
Description
FIGURES
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[0169] Lefta comparison with starting material, where (a) is HY5.1, (b) is HY5.1 @ LDH-A and (c) is LDH-A. [0170] Righta comparison between water- and acetone-washed samples, where (a) is HY5.1 @ LDH-W and (b) is HY5.1 @ LDH-A. LDH-W denotes conventionally synthesised LDH, LDH-A denotes AMO-synthesised LDH.
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EXAMPLES
[0206] Experimental Methods [0207] 1. General Details [0208] 1.1 Powder X-Ray Diffraction [0209] Powder X-ray diffraction (XRD) data were collected on a PANAnalytical XPert Pro diffractometer in reflection mode and a PANAnalytical Empyrean Series 2 at 40 kV and 40 mA using Cu K radiation (1=1.54057 , 2=1.54433 , weighted average=1.54178 ). Scans were recorded from 50 70 with varying scan speeds and slit sizes. Samples were mounted on stainless steel sample holders. The peaks at 43-44 are produced by the XRD sample holder and can be disregarded. [0210] 1.2 Thermogravimetric Analysis [0211] Thermogravimetric analysis (TGA) measurements were collected using a Netzsch STA 409 PC instrument. The sample (10-20 mg) was heated in a corundum crucible between 30 C. and 800 C. at a heating rate of 5 C. min.sup.1 under a flowing stream of nitrogen. [0212] 1.3 Transmission Electron Microscopy [0213] Transmission Electron Microscopy (TEM) analysis was performed on a JEOL 2100 microscope with an accelerating voltage of 200 kV. Particles were dispersed in water or ethanol with sonication and then cast onto copper grids coated with carbon film and left to dry. [0214] 1.4 Brunauer-Emmett-Teller Surface Area Analysis [0215] Brunauer-Emmett-Teller (BET) specific surface areas were measured from the N.sub.2 adsorption and desorption isotherms at 77 K collected from a Quantachrome Autosorb surface area and pore size analyser. [0216] General Method of Synthesis [0217] Zeolite was dispersed in deionised water using ultrasound treatment. After 30 minutes, sodium carbonate was added to the solution and a further 6 minutes of sonication was carried out to form solution A. An aqueous solution containing magnesium nitrate hexahydrate and aluminium nitrate nonahydrate was added at a rate to solution A under vigour stirring. The pH of the reaction solution was controlled with the addition of 1 M NaOH by an autotitrator. The obtained suspension was stirred for 1 h. Optionally, the obtained solid was collected and then re-dispersed in deionised water and stirred for 1h. The samples (Zeolite @ LDH) were then dried under vacuum. The Zeolite @ AMO-LDH was synthesized using the same procedure. However, before final isolation, the solid was treated with AMOST method, which was washed with acetone and then re-dispersed in a fresh acetone under stirring for certain time. The solid was then dried under vacuum for materials characterization. [0218] Using this general method, zeolite @ LDH shell materials were synthesised using the different zeolite types HY5.1, HY30, HY15, syn-ZSM5, ZSM5-23 and ZSM5-40. [0219] Experimental Methods [0220] Example Method of HY5.1 @ LDH [0221] HY5.1 (100 mg) was dispersed in deionised water (20 mL) using ultrasound treatment. After 30 minutes, sodium carbonate was added to the solution and a further 6 minutes of sonication was carried out to form solution A. An aqueous solution (19.2 mL) containing magnesium nitrate hexahydrate and aluminium nitrate nonahydrate was added at a rate of 60 ml/h to solution A under vigour stirring. The pH of the reaction solution was controlled with the addition of 1 M NaOH by an autotitrator. The obtained suspension was stirred for 1 h. Optionally, the obtained solid was collected and then re-dispersed in deionised water (40 mL) and stirred for 1 h. The collection and re-dispersion was repeated once. The samples (HY5.1 @ LDH) were then dried under vacuum. The HY5.1 @ AMO-LDH was synthesized using the same procedure. However, before final isolation, the solid was treated with AMOST method, which was washed with acetone (40 mL) and then re-dispersed in a fresh acetone (40 mL) under stirring for overnight. The solid was then dried under vacuum for materials characterization. [0222] The zeolite @ LDH shell materials obtained using these different zeolite types were characterised and/or studied according to the following. [0223] Characterisation of HY5.1 @ LDH [0224] The zeolite HY5.1 was used to attempt the synthesis of the first Zeolite @ AMO-LDH.
[0232] Variation of Zeolite to LDH Ratio in HY15 @ AMO-LDH [0233]
TABLE-US-00001 TABLE 1 Summary data from N.sub.2 adsorption and desorption BET External Micropore Micropore Cumulative SSA SSA SSA volume Volume Samples (m.sup.2/g) (m.sup.2/g) (m.sup.2/g) (cc/g) (cc/g) HY5.1 813 72 740 0.28 0.08 HY5.1@LDH-W 565 164 401 0.17 0.60 HY5.1@LDH-W 698 497 LDH-W 11 0.4 11 0.004 0.04 LDH-A 281 252 29 0.01 1.08 ZSM5-23 424 45 379 0.15 0.05 ZSM5-23@LDH- 167 54 113 0.04 0.33 W ZSM5-23@LDH-A 339 140 199 0.08 0.05 HY5.1 300 C. 695 70 625 0.30 0.07 HY5.1@LDH-A 698 201 497 0.23 0.66 300 C. [0242] LDH-W means the LDH was prepared by the conventional method in water. [0243] LDH-A means the LDH was treated with acetone.
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[0274] While specific embodiments of the invention have been described herein for the purpose of reference and illustration, various modifications will be apparent to a person skilled in the art without departing from the scope of the invention as defined by the appended claims.