Method for making LaCO3OH nanoparticles from aqueous salt solutions
10512900 ยท 2019-12-24
Assignee
Inventors
Cpc classification
C01P2004/61
CHEMISTRY; METALLURGY
C01P2002/76
CHEMISTRY; METALLURGY
C01F17/30
CHEMISTRY; METALLURGY
B01D53/9413
PERFORMING OPERATIONS; TRANSPORTING
B01J37/0072
PERFORMING OPERATIONS; TRANSPORTING
B01J37/10
PERFORMING OPERATIONS; TRANSPORTING
C01P2002/88
CHEMISTRY; METALLURGY
C01P2002/60
CHEMISTRY; METALLURGY
C01P2002/70
CHEMISTRY; METALLURGY
B01D53/8628
PERFORMING OPERATIONS; TRANSPORTING
B01J35/30
PERFORMING OPERATIONS; TRANSPORTING
C01P2004/62
CHEMISTRY; METALLURGY
C01P2002/77
CHEMISTRY; METALLURGY
F01N3/2825
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
C01P2002/72
CHEMISTRY; METALLURGY
International classification
B01J37/03
PERFORMING OPERATIONS; TRANSPORTING
B01J37/10
PERFORMING OPERATIONS; TRANSPORTING
B01J37/00
PERFORMING OPERATIONS; TRANSPORTING
B01J35/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A hydrothermal method of preparing uniform, monodisperse ceramic lanthanum hydroxyl carbonate (LaCO.sub.3OH) having cherry-blossom-like nanogears and/or nanocubes is described. The method produced a hexagonal crystal with a crystal lattice in which at least on lanthanum ion is substituted with calcium ion. The ceramic nanoparticles produced by the method are good catalyst for the reduction of nitrogen oxides with a hydrocarbon. A method of reducing exhaust gases is described.
Claims
1. A method of forming lanthanum hydroxycarbonate nanoparticles having a crystal lattice structure, wherein at least one lanthanum cation of the crystal lattice structure is substituted with a calcium cation, said method comprising: forming an aqueous reaction mixture by combining an aqueous solution of a lanthanum salt with an aqueous solution of a calcium salt to form a mixed solution, then combining the mixed solution with a aqueous solution of an ammonium carbonate, hydrothermally treating the aqueous reaction mixture comprising water, the calcium salt, the lanthanum salt, and the ammonium carbonate salt at a temperature of 120 to 250 C. for a time of 12-60 hours to form the ceramic nanoparticles, wherein a molar ratio of lanthanum to calcium is in the range of 80:20 to 99:1.
2. The method of claim 1, wherein the aqueous hydrothermal reaction mixture does not contain a templating agent or a catalyst, and wherein the aqueous hydrothermal reaction mixture has a pH in the range of 7.5 to 10.0.
3. The method of claim 1, wherein the molar ratio of lanthanum to calcium is in a range 80:20 to 95:5.
4. The method of claim 1, wherein the molar ratio of lanthanum to calcium is 95:5.
5. The method of claim 1, wherein the crystal lattice is hexagonal.
6. The method of claim 5 wherein the hexagonal crystal lattice has a unit cell dimension of unit cell dimension of a=b=1.260.16 nm and c=1.000.1 nm.
7. The method of claim 1, wherein the ammonium carbonate salt is at least one selected from the group consisting of ammonium carbonate, alkylammonium carbonate, dialkylammonium carbonate, and trialkylammonium carbonate, and wherein the alkylgroup is at least one selected from the group consisting of methyl, ethyl, propyl, isopropyl, butyl, and isobutyl.
8. The method of claim 1, wherein the temperature is in a range of 120-200 C.
9. The method of claim 1, wherein the time is in a range of 12-48 hours.
10. The method of claim 1, wherein the molar ratio of lanthanum to calcium is in the range 80:20 to 95:5, the ammonium salt is ammonium carbonate, and the time is in a range 12-48 hours.
11. The method of claim 1, wherein the nanoparticles have morphology of nanogear with a cherry-blossom-like structure or a nanocube.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) A more complete appreciation of the disclosure and many of the attendant advantages thereof will be readily obtained as the same becomes better understood by reference to the following detailed description when considered in connection with the accompanying drawings, wherein:
(2)
(3)
(4)
(5)
(6)
(7)
(8)
(9)
(10)
(11)
(12)
(13)
(14)
DETAILED DESCRIPTION OF THE EMBODIMENTS
(15) Embodiments of the present disclosure will now be described more fully hereinafter with reference to the accompanying drawings, in which some, but not all embodiments of the disclosure are shown.
(16) All publications mentioned herein are incorporated herein by reference in full for the purpose of describing and disclosing the methodologies, which are described in the publications, which might be used in connection with the description herein. The publications discussed above and throughout the text are provided solely for their disclosure prior to the filing date of the present application. Nothing herein is to be construed as an admission that the inventors are not entitled to antedate such disclosure by virtue of prior disclosure. Also, the use of or means and/or unless stated otherwise. Similarly, comprise, comprises, comprising include, includes, and including are interchangeable and not intended to be limiting.
(17) The present disclosure will be better understood with reference to the following terms and meanings set forth below. Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood to one of ordinary skill in the art.
(18) As used herein, the words a and an and the like carry the meaning of one or more. Within the description of this disclosure, where a numerical limit or range is stated, the endpoints are included unless stated otherwise. Also, all values and subranges within a numerical limit or range are specifically included as if explicitly written out.
(19) As used herein, compound is intended to refer to a chemical entity, whether as a solid, liquid, or gas, and whether in a crude mixture or isolated and purified.
(20) As used herein, a composite is intended to refer to a solid material comprising more than one phase and/or compound.
(21) As used herein, a nanocomposite is intended to refer to a composite wherein the phase and/or compound domains have one or more dimensions of 100 nanometers (nm) or less, and/or repeat distances of 100 nm or less.
(22) The term multiphasic, as used herein, refers to a compound comprising two or more types of amorphous and/or crystalline phases. Biphasic compounds and triphasic compounds may be referred to as multiphasic compounds.
(23) The term alkyl, as used herein, unless otherwise specified, refers to a saturated straight, branched, or cyclic, primary, secondary, or tertiary hydrocarbon of typically C1 to C8, and specifically includes methyl, ethyl, propyl, isopropyl, cyclopropyl, butyl, isobutyl, 1-butyl, pentyl, cyclopentyl, isopentyl, neopentyl, hexyl, isohexyl, cyclohexyl, cyclohexylmethyl, 3-methylpentyl, 2,2-dimethylbutyl, 2,3-dimethylbutyl, and octyl. The term optionally includes substituted alkyl groups. Moieties with which the alkyl group can be substituted are selected from the group consisting of hydroxyl, amino, halogen, alkylamino, arylamino, alkoxy, aryloxy, nitro, cyano, sulfonic acid, sulfate, phosphonic acid, phosphate, or phosphonate, either unprotected, or protected as necessary, as known to those skilled in the art, for example, as taught in Greene, et al., Protective Groups in Organic Synthesis, John Wiley and Sons, Second Edition, 1991, hereby incorporated by reference in its entirety.
(24) The present disclosure is intended to include all isotopes of atoms occurring in the present compounds and complexes. Isotopes include those atoms having the same atomic number but different mass numbers. By way of general example and without limitation, isotopes of hydrogen include deuterium and tritium. Isotopes of carbon include .sup.13C and .sup.14C. Similarly, lanthanum isotopes include the stable and most abundant isotope .sup.139La and the radioactive .sup.138La, .sup.137La, and .sup.140La as well as all other 35 short lived isotopes .sup.117-136 and 140-155La. Also, calcium has several known stable isotopes including .sup.40Ca, .sup.42Ca, .sup.43Ca, .sup.44Ca, and .sup.46Ca as well as unstable isotopes including .sup.41Ca, .sup.45Ca, .sup.47Ca, and .sup.48Ca. Isotopically-labeled compounds of the disclosure can generally be prepared by conventional techniques known to those skilled in the art or by processes analogous to those described herein, using an appropriate isotopically-labeled reagent in place of the non-labeled reagent otherwise employed.
(25) According to first aspect, the present disclosure relates to a method of fabricating a ceramic nanoparticle of lanthanum hydroxycarbonate with a crystal lattice structure, wherein at least one lanthanum cation of the crystal lattice structure is substituted with a calcium cation. Said nanoparticle has a morphology selected from the group consisting of flower like morphology, a nanogear morphology, and a nanocubic morphology. The method comprises hydrothermally treating a reaction mixture of aqueous solution comprising a calcium salt, a lanthanum salt, and ammonium carbonate at a temperature of 150 to 250 C. for 12-60 hours to form the ceramic nanoparticle, wherein a molar ratio of lanthanum to calcium is in the range of 80:20 to 99:1.
(26) One of ordinary skill in the art would appreciate that any organic or inorganic salt of lanthanum and/or calcium can be used as a reaction mixture in the method. For example, lanthanum or calcium nitrate, nitrite, sulfate, or halides such as fluoride, chloride, bromide, or iodide or mixtures thereof can be utilized in the method. Also, lanthanum and calcium salts of organic acids such as formic acid, acetic acid, propionic acid, butyric acid, oxalic acid, tartaric acid, lactic acid or citric acid may be used. In a preferred embodiment, the salts are inorganic salts selected from the group consisting of lanthanum and/or calcium nitrate, nitrite, sulfate, or halides such as fluoride, chloride, bromide, or iodide or mixture thereof. In the most preferred embodiment, salts are lanthanum nitrates and calcium nitrate. The salts can be hydrated or non-hydrated and when solvated may contain organic solvent such as methanol, ethanol, or acetonitrile. More than one lanthanum or calcium salts may be used in the method.
(27) The molar ratio of lanthanum salt to calcium salt can vary depending on the desired ceramic nanoparticle morphology and characteristics. In one embodiment the molar ratio is 80:20, 85:15, 90:10, 91:9, 92:8, 93:7, 94:6, 95:5, 96:4, 97:3, 98:2, or 99:1, or any intermediate ranges there between. In a preferred embodiment, the molar ratio ranges from 90:10 to 99: I. In the more preferred embodiment, the molar ratio is 80:20, 85:15, 90:10, 93:7, 94:6, 95: 5, 96:4, or 97:3. In the most preferred embodiment, the molar ratio is 95:5.
(28) The fabrication method of the nanoparticle may be carried out on any scale as long as the lanthanum salt and calcium salt are dissolved in water. Lanthanum salts and calcium salts have similar solubility in water. For example, the solubility of both lanthanum nitrate and calcium nitrate are about 136 g/100 ml at ambient temperature. So, the method can be carried out on a laboratory scale, i.e., <1 g of lanthanum nitrate in a volume ranging from 1-15 ml, or on much larger scale of up to 1.36 kg in a volume of one liter and multiples thereof. Any carbonate or bicarbonate salt of ammonia or amines can be employed. Examples of the carbonate or bicarbonate salts to be used are ammonium carbonate, ammonium bicarbonate, alkyl, dialkyl, or trialkylammonium carbonate or bicarbonate wherein the alkyl group is an optionally substituted methyl, ethyl, propyl, isopropyl, butyl, aryl or heteroaryl. In a preferred embodiment, ammonium carbonate and/or ammonium bicarbonate is added to the mixture. The amount of carbonate salt should be added to the reaction mixture in sufficient quantity to allow the co-precipitation of the metal ions and it can be added in large molar excess to the lanthanum salt. The carbonate salt may be added to the reaction mixture in molar equivalent to the lanthanum salt or in the range of 1-100 times, 5-50 times, 10-40 times, or 20-30 times the molar amount of the lanthanum salt. The reaction mixture is maintained at a pH between 7.0-10.0, preferably between 7.5-9.5, more preferably between 8.0-9.0, and even more preferably between 8.0-8.5. In the most preferred embodiment, the pH of the reaction mixture is maintained at 8.0 by adding acid or base. The water used in the reaction mixture may be tap water, distilled water, twice distilled water, deionized water, deionized distilled water, reverse osmosis water, and/or some other water. In one embodiment the water is twice distilled to eliminate trace metals. Preferably the water is twice distilled, deionized, deionized distilled, or reverse osmosis water and at 25 C. has a conductivity at less than 10 S.Math.cm.sup.1 preferably less than 1 S.Math.cm.sup.1, a resistivity greater than 0.1 M.Math.cm, preferably greater than 1 M.Math.cm, more preferably greater than 10 M.Math.cm, a total solid concentration less than 5 mg/kg, preferably less than 1 mg/kg, and a total organic carbon concentration less than 1000 g/L, preferably less than 200 g/L, more preferably less than 50 g/L.
(29) The reaction mixture may be sonicated for at least 20 minutes, preferably at least 40 minutes, more preferably at least 60 minutes, using a sonication bath or a sonication probe to produce a sonicated mixture prior to the hydrothermal treatment. Alternatively, the mixture may not be sonicated but instead mixed, stirred, rocked, and/or agitated for an equivalent amount of time. In an alternative embodiment, the mixture may only be mixed to form a homogeneous mixture, and then left to sit for the previously mentioned amount of time.
(30) The sonicated mixture may be aged, or left to sit unperturbed, for at least 12 h, preferably at least 24 h, more preferably at least 48 h at 18-37 C., preferably 20-30 C., more preferably 21-27 C. In an alternative embodiment, the sonicated mixture may be mixed, stirred, rocked, and/or agitated for an equivalent time and at an equivalent temperature.
(31) The temperature of the hydrothermal treatment can vary between 150 to 250 C., preferably 160 to 200 C., more preferably 170 to 190 C., and even more preferably 180 to 185 C. In the most preferred embodiment, the temperature maintained at 180 C. Also, the duration of the hydrothermal treatment can vary between 12-72 h, preferably 12-60 h, and more preferably 12-48 h. In the most preferred embodiment, the duration of the hydrothermal treatment is selected from the group consisting of 12, 20, 24, and 48 hours.
(32) One main advantages of the hydrothermal method described herein are that the ceramic nanoparticle is formed without the assistance of a template or catalyst at relatively low temperature and coast with well-defined morphology. Another advantage is that the method produced the more stable hexagonal crystal lattice of LaCO.sub.3OH in which at least one lanthanum ion is replaced with calcium ion. As used herein, the term template refers to as a structure directing agent and is stable under hydrothermal aging conditions and furthermore hydrophobic relative to the metal salts. Many templates used in the manufacturing nanoparticles are known in the art. They include all types of surfactants including anionic surfactants, cationic surfactants, and neutral surfactants. The surfactant may act as a nucleation site for the formation of the nanoparticles. Alkyl ammonium salts are commonly used as templates to form structures in solution that interacts with the inorganic material in solution and serve as a template for the growth of nanoparticles. A commonly used template is tetrapropylammonium hydroxide, tetraethylammonium hydroxide, tetrabutylammonium hydroxide, or tetrapentylammonium hydroxide. Other known templates include cetyl trimethylammonium bromide, cetyl triethylammonium bromide, or dodecyl triethylammonium bromide, Pluronic F127, Pluronic P123, Brij-56, or Brij-30. The template is usually decomposed during calcining at temperatures in the range 545-600 C. for 6-10 hours. Similarly, the term catalyst in the context of nanoparticle formation refers to any organic or inorganic molecule(s) or combination thereof that enhances or accelerates the formation of nano-particles. Examples of such a catalyst include, but are not limited to polyols such as ethylene glycol, glycerol, polyetheleneglycol (PEG), and urea.
(33) A second aspect of the invention is the ceramic nanoparticle of lanthanum hydroxycarbonate with a crystal lattice structure, wherein at least one lanthanum cation of the crystal lattice structure is substituted with a calcium cation prepared by the hydrothermal method described herein. The nanoparticle may have any morphology as long as at least one lanthunm ion is substituted with calcium ion. A preferred embodiment, the nanoparticle has flower-like morphology, a nanogear morphology, and a nanocubic morphology, double-decker-like microhexagrams morphology, spiky balls morphology, triangular hearts morphology, apple-like nanostructures, microspheres, nanowires, the layer-by-layer self-assembly of nanoplates, and combination thereof. A preferred embodiment, the ceramic nanoparticle is selected from the group consisting of flower-like morphology, a nanogear morphology, and a nanocubic morphology. A more preferred embodiment, the ceramic nanoparticle has a flower-like morphology or cubic morphology. An even more preferred embodiment, the ceramic nanoparticle has a nanogear morphology. In the most preferred embodiment, the nanoparticle has an X-ray diffraction pattern consistent with hexagonal crystal with unit cell dimension of a=b=1.260.16 nm and c=1.00 0.1 nm. The result of the X-ray diffraction experiment indicates that calcium ions partially and/or totally La.sup.43 host lattice site. It should be noted that the ionic radius of calcium ion (0.99 ) is very similar to that of La ion (1.061 ). In another embodiment, the nanoparticle has nanogear morphology and a broad fluorescent emission maximum at 399 nm.
(34) The La(CO.sub.3)OH nanoparticles are uniform in shapes and sizes. The average length of the particle is in the range of 0.5-10.0, preferably 1.0-5.0, 1.5-4.0, or 1.5-3.0 m, and preferably 1.5-2.0 m. The average thickness of the particle is in the range of 0.20-1.50, preferably 0.30-1.30, 0.4-1.10, 0.5-1.0, 0.6-0.90, or 0.70-0.80 m, preferably 0.75 m. The nanoparticles can appear like cubes of ice or prisms resembling nanogears. The cross section of the nanogear can be triangular or circular in shape and has teeth-like structure at the corners of the triangle or the edge of the circle (see for example
(35) A third aspect of the invention is directed to a method of reducing nitrogen oxides such as NO and NO.sub.2 in a gas stream to nitrogen with a hydrocarbon. The gas stream may contain any amount of nitrogen oxides. In a preferred embodiment of the invention, the nitrogen oxide is at concentration in the range of 10-10,000 ppm, preferably, in the range of 100-5000 ppm, more preferably, in the range 500-3000, and most preferably in the range of 1000-2000 ppm. The hydrocarbon can be any hydrocarbon such as methane, ethane, propane, propene, butane, isobutane, butene, isobutene, pentane, cyclopentane, cyclopentene, hexane, hexane, cyclohexane, cyclohexene, or any isomer thereof. The gas stream may have water content in the range of 0%-20% water, preferably in the range of 1%-15%, more preferably 1%-10%, and most preferably 2%-10%. Similarly, the stream of gas may contain oxygen in an amount in the range 0%-20%, preferably in the range 5%-15%, and more preferably, in the range 5%-10%. The effect of water on the catalyst is small and reversible (see
(36) The examples below are intended to further illustrate protocols for preparing, characterizing, and using a multiphasic titanium dioxide photocatalyst, and are not intended to limit the scope of the claims.
Example 1
(37) Analytical Methods:
(38) X-ray diffraction (XRD) analyses were performed on a Bruker D8 Advance diffractometer system with an operating voltage of 40 kV and a current of 40 mA by using Cu K radiation (=1.5405 ) and a graphite monochromator. The samples were investigated over the 28 range 10-80 at a scanning speed of 2 min.sup.1. Fourier transform infrared (FT-IR) spectra were collected on a Bruker FT-IR spectrometer by using the KBr pellet technique. Thermal gravimetric analysis (TGA) analyses were carried out using a thermogravimetric analyzer (Discovery, TA, USA). A 5.0 mg sample was placed in an aluminum pan and heated from 30 to 600 C. under N.sub.2 at a heating rate of 10 C./min. The morphologies and sizes of the resulting products were determined with field emission scanning electron microscopy (TESCAN LYRA3, Czech Republic). TEM images were recorded by using a transmission electron microscope (JEOL, JEM 2011) operated at 200 kV with a 4 k4 k CCD camera (Ultra Scan 400SP, Gatan). PL measurements were performed with a spectrofluorometer (Fluorolog FL3-iHR, HORIBA Jobin Yvon, France). The chemical compositions of the samples were determined with X-ray photoelectron spectroscopy (XPS) by using an X-ray photoelectron spectrometer (ESCALAB-250, Thermo-VG Scientific) with AlK radiation (1486.6 eV).
Example 2
(39) Hydrothermal Method for the Synthesis of LaCO.sub.3OH:
(40) A reaction mixture of La(NO.sub.3).sub.3.6H.sub.2O Sigma-Aldrich Co.) and Ca(NO.sub.3).sub.2.4H.sub.2O (Fluka) in a molar ratio of 95:5 is obtained by mixing solutions of La(NO.sub.3).sub.3 and Ca(NO.sub.3).sub.2 dissolved in deionized water. To the reaction mixture, a sufficient amount of (NH.sub.4).sub.2CO.sub.3 solution (4.1 mol/ml, Merck) is added to co-precipitate the metal ions by adjusting the pH to about 8.5. In a typical preparation, 1 ml solution of 6.8 mg (0.029 mmol) of Ca(NO.sub.3).sub.2 in water is added to 15 ml solution of 0.25 g (0.57 mmol) of La(NO.sub.3).sub.3.6H.sub.2O in water followed by the addition of 0.017 mol (NH.sub.4).sub.2CO.sub.3 solution. The pH of the reaction mixture is adjusted to about 8.5 with ammonium carbonate and the reaction mixture is incubated and vigorously stirred for 12 hours while maintaining the pH at about 8.5 by adding NH.sub.3.H.sub.2O (25 wt %) or a HNO.sub.3 (1 M) solution. The reaction mixture is transferred to a plastic container with an inner volume of 500 ml, and then the plastic container was inserted into a steel vessel. The mouth of the vessel was closed, and the hydrothermal reactions were performed at 180 C. for more than 48 h, 24 h, and 12 h to produce the samples LC-48, LC-24, and LC-12, respectively. The resulting powders were washed three times with alcohol, deionized water, and dried at 110 C. Using the same procedure, nanoparticles containing molar ratio of La:Ca=80:20, La:Ca=85:15, and La:Ca=90:10 nanoparticles were synthesized. An autoclave with a capacity of 500 mL and a magnetically driven stirrer were used in the hydrothermal reactions. The resulting powders were washed three times with alcohol, deionized water, and dried at 110 C.
Example 3
(41) Characterization of the Nanoparticles:
(42) (a) X-Ray Diffraction:
(43)
(44) (b) Field Emission Scanning Electron Microscopy (FE-SEM):
(45) The surface morphologies of all samples were examined by using FE-SEM after applying an Au coating. The FE-SEM images in
(46) (c) Transmission Electron Microscopy (TEM):
(47) The TEM image of the LC-24 sample shows that is has a clear morphology with a cubic structure [
(48) (d) FTIR:
(49)
(50) (e) Surface Composition and Oxidation State:
(51) The surface compositions and oxidation states of the samples were characterized by using XPS.
(52) The present disclosure describes a synthetic method based on the control of the La and Ca molar ratio for the fabrication of a phase-pure LaCO.sub.3OH nanogear structure. A broad O 1s XPS peak corresponding to lattice oxygen is present at 531.5 eV in the spectrum of the as-prepared sample [Xia et al. Morphology-Controllable Synthesis and Characterization of Single-Crystal Molybdenum Trioxide, J. Phys. Chem. B, 110 (2006) 2006-2012]. The two peaks at 289.6 eV and 284.60 eV in the C 1s spectrum (
(53) The effect of experimental parameters on the morphology of LaCO.sub.3OH was examined. Most of the reported unique morphologies of LaCO.sub.3OH have been obtained using organic additive. Li et al. [Eu.sup.3+/Tb.sup.3+-Doped La.sub.2O.sub.2CO.sub.3/La.sub.2O.sub.3 Nano/Microcrystals with Multiform Morphologies: Facile Synthesis, Growth Mechanism, and Luminescence Properties, Inorg. Chem. 49 (2010) 10522-10535] investigated the effects of using NaHCO.sub.3, NH.sub.4HCO.sub.3, Na.sub.2CO.sub.3, (NH.sub.4).sub.2CO.sub.3, and CO(NH.sub.3).sub.2 as carbon sources and found that the XRD peaks of all samples could be indexed as the pure orthorhombic LaCO.sub.3OH phase, which indicates that using a different carbon source does not change the crystal phase of the product. This was not true after an addition of small amount of Ca.sup.2+ in the present study. In this study, we obtained a pure hexagonal LaCO.sub.3OH phase instead of orthorhombic with a unique cherry blossom morphology by keeping all other parameters are fixed. Of course, the reaction temperature had a significant influence on the crystal phase formation and the morphology. By increasing the reaction time i.e., more than 20 h, nanogears are more visible under hydrothermal reaction conditions. Which is completely different in presence of a polymer additive during the synthesis of nanogears LaCO.sub.3OH [Zhang et al. RSC Adv. 5 (2015) 21925-21950]. Thus, Ca.sup.2+ plays a significant role for both the phase and new morphology formation. The morphology of molybdenum trioxide was also controlled using Ca(NO.sub.3).sub.2 and La(NO.sub.3).sub.3 via a facile hydrothermal method [Kanari et al. Thermal decomposition of zinc carbonate hydroxide, Thermochim. Acta 410 (2004) 93-100]. The effect of Ca.sup.2+ content was examined on morphology of other molar ratios of La:Ca for example La:Ca=90:10, La:Ca=85:15, and La:Ca=80:20 samples under the same hydrothermal conditions [
(NH.sub.4).sub.2CO.sub.3 (aq).fwdarw.2NH.sub.4.sup.++CO.sub.3.sup.2(1)
NH.sub.4.sup.++H.sub.2O (l).Math.NH.sub.3(aq)+H.sub.3O.sup.+(2)
CO.sub.3.sup.2+H.sub.2O (l).Math.HCO.sub.3.sup.+OH.sup.(3)
La.sup.3++OH.sup.+CO.sub.3.sup.2.fwdarw.LaCO.sub.3OH(4)
(54) In contrast to urea, the carbon source, i.e., (NH.sub.4).sub.2CO.sub.3 is completely ionized and solvated in water as NH.sub.4.sup.+ and CO.sub.3.sup.2 ions which provides a good quantity of CO.sub.3.sup.2 and OH.sup. ions. Most of the NO.sub.3.sup. was washed off during cleaning step. The strong affinity between La.sup.+ and CO.sub.3.sup.2 was led to the formation of LaCO.sub.3 [Gaines et al. (1997) Dana's New Mineralogy, 8th ed, John Wiley & Sons: New York, Class 15 and 16]. Initially, the particles growth rate was faster along an axis due to the presence of high concentration of CO.sub.3.sup.2 and OH.sup., according to the proposed mechanism by Peng et al. [Shape control of CdSe nanocrystals, Nature, 404 (2000) 59-61], and Ca.sup.2+ might be absorbed at the same time on the LaCO.sub.3 crystal faces, which hinder the rod-like particles formation. Also, the presences of CO.sub.2 and NH.sub.3 micro-gas bubbles in the growth process may lead to tiny gaps on the surface and on the inner portion of the nanogears. Consequently, the Ca.sup.2+ absorption is enhanced and Ca.sup.2+ ions penetrate in different direction. Finally, the overall growth rate could be slow under hydrothermal conditions and this situation favored the cherry blossom type short size nanogears morphology formation.
(55) (d) Luminescence Properties of the Nanoparticles:
(56) The effects of morphology/crystallinity on the photoluminescence (PL) emission intensities were examined.
Example 4
(57) Catalytic Activity of Nanoparticles:
(58) Method of Reduction of Nitrous Oxide:
(59) A pyrex glass tubular reactor with an internal diameter of 12 mm was used in the catalytic performance tests. The nanoparticles samples were retained between glass wool plugs in the reactor. The gas flow rate is controlled with a mass flow controller at predetermined flow rate. A 4-channel electronic mass-flow controller was used to fix the total flow rate at a constant value. The furnace temperature was increased at a linear heating rate of approx. 10 Kmin.sup.1 with a computer-based temperature controller. Before performing the tests, the total system was activated by increasing the temperature from 200 to 800 C. under real feed conditions. Data was collected during cooling from 700 to 200 C. every 60 C. after 40 min stabilization at each selected temperature point. During the H.sub.2O vapor test, 10% H.sub.2O vapor was inserted into the gas mixture with a micro-pump. The catalytic activities were determined in a flowing gas containing 1000-2000 ppm NO, 5% O.sub.2, and 2-10% H.sub.2O diluted in He; catalysts weight 0.18 g; GHSV (gas hour space velocity): 2000 h.sup.1. Gas chromatography and a molecular sieve were used to analyze the effluent gas at intervals of 20 min. By using an empty catalyst test station, an experiment was performed by flowing the original feed to verify that no NO.sub.x reduction occurs in the absence of catalyst.
(60) NO and hydrocarbon conversion were calculated based on the hydrocarbon intake to obtain the NO reduction percentage. The NO conversion and the hydrocarbon conversion to CO.sub.x (CO+CO.sub.2) were calculated based on the following expressions. The percentage error in the calculation data should be less than 2%.
NO conversion to N.sub.2 (%)={2[N.sub.2]/[NO].sup.in}100
CH.sub.4 conversion to CO.sub.2 (%) {()[CO.sub.2]/[CH.sub.4].sup.in}100
C.sub.3H.sub.6 conversion to CO.sub.2(%)={()[CO.sub.2]/[C.sub.3H.sub.6].sup.in}100
The 3.sup.rd bracket denotes the feed concentration, and [NO].sup.in, [CH.sub.4].sup.in or [C.sub.3H.sub.6].sup.in are the initial concentrations of NO, CH.sub.4 or C.sub.3H.sub.6 respectively. [N.sub.2] and [CO.sub.2] are the final (after testing) concentrations of N.sub.2 and CO.sub.2.
(61)
(62) Both samples had very low surface area but their particles size, shape and surface morphologies were very different. Costa et al. [The Selective Catalytic Reduction of Nitric Oxide with Methane over La.sub.2O.sub.3CaO Systems: Synergistic Effects and Surface Reactivity Studies of NO, CH.sub.4, O.sub.2, and CO.sub.2 by Transient Techniques, J. Catal. 194 (2000) 250-265] reported very low surface area of 7 m.sup.2/g for the same LaCa (95-5 wt %) sample after heat treatment at 300 C., although the NO reduction activity was performed in the 400-800 C. range. They prepared the LaCa (95-5 wt %) sample by mixing two oxide powders at 60 C. On the other hand, hydrothermally prepared LC-24 nanocubes were prism like particles and no physical water molecules were attached as evidenced by very weak OH group in the FTIR spectra [
(63) NO reduction activities were slightly decreased in the case of La:Ca=90:10, La:Ca=85:15, and La:Ca=80:20 samples. The low activity of La:Ca=90:10, La:Ca=85:15, and La:Ca=80:20 samples probably due to agglomerated morphology with undefined structure as shown in
(64) The catalytic activity of LC-24 catalysts was tested using two types of reducing agent CH.sub.4 and C.sub.3H.sub.6 in the presence of oxygen [
(65) Effect of Water on the Catalytic Activity of Nanoparticles:
(66) The exhaust gas is mainly consists of NO, NO.sub.2, CO.sub.2, CO, H.sub.2O and O.sub.2. Most of the cases the catalytic activity decreased severely in the presence of H.sub.2O vapor (Zahir et al.). Therefore, we have tested the performance of LC-24 powders in presence of H.sub.2O vapor; however, it was observed that the obstructing effect of 10% H.sub.2O in the feed stream is small as shown in
(67) The XRD pattern shows the presence of mostly hexagonal La.sub.2O.sub.3 (JCPDS 05-0602) phase after heat treatment the LaCO.sub.3OH sample i.e., LC-24 nanocube powders. The final products were pure La.sub.2O.sub.3, a mixture La.sub.2O.sub.3 of La(OH).sub.3 and small amount of La.sub.2O.sub.2CO.sub.3, which were characterized by XRD shown in
(68) La was used for the preparation of luminescent and catalyst materials. La mineral resources are plentiful and La.sub.2O.sub.3 is relatively cheap in comparison to other rare earth minerals. Although the supply of La remains in excess of demand in the RE industry, the availability of La-based materials are still scarce. Herein is described the synthesis of LaCO.sub.3OH with cubic and nanogear-type morphologies that does not require the assistance of templates or catalysts. The large-scale production of phase-pure hexagonal LaCO.sub.3OH is achieved by using a simple and environmentally friendly hydrothermal method. This synthesis route provides a general approach to the synthesis of rare-earth compounds with a variety of morphologies and properties. High durability was observed for the reduction of NO by CH.sub.4 in the presence of water vapor, maintaining a high stability over 100 h.