KR101840534B1 - Reactor - Google Patents
Reactor Download PDFInfo
- Publication number
- KR101840534B1 KR101840534B1 KR1020160016377A KR20160016377A KR101840534B1 KR 101840534 B1 KR101840534 B1 KR 101840534B1 KR 1020160016377 A KR1020160016377 A KR 1020160016377A KR 20160016377 A KR20160016377 A KR 20160016377A KR 101840534 B1 KR101840534 B1 KR 101840534B1
- Authority
- KR
- South Korea
- Prior art keywords
- metal
- metal precursor
- reaction
- formula
- nanoparticles
- Prior art date
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/087—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/087—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
- B01J19/088—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy giving rise to electric discharges
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/10—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing sonic or ultrasonic vibrations
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/26—Nozzle-type reactors, i.e. the distribution of the initial reactants within the reactor is effected by their introduction or injection through nozzles
Abstract
According to the reactor of the present application, the solution containing the metal precursor is injected into a solution containing a reactive compound having a very high reactivity with the metal precursor to suppress the explosion reaction rate of the metal nanoparticle precursor , The particle size of the precursor nanoparticles can be controlled to be small even at a small cost, and thus a film having a uniform surface roughness can be produced in a large area.
Description
The present application relates to a reactor capable of controlling the rate of reaction of highly reactive compounds.
Gallium nitride is a semiconductor material with a wide band gap energy of 3.4 eV, direct band transfer, high energy radiation and high stability to high temperatures. Given these properties, gallium nitride is known as a promising material for light emitting diodes, short wavelength lasers, UV detectors and solar cell windows in space.
For example, the gallium nitride film may be formed by mixing a solution containing a gallium precursor and a solution containing sodium dimethyldithiocarbamate to form metal precursor nanoparticles, then coating the nanoparticles on the substrate and heat-treating However, since the gallium precursor and sodium dimethyldithiocarbamate have very high reactivity, an explosive reaction occurs when the gallium precursor and sodium dimethyldithiocarbamate are simply mixed. Therefore, the metal precursor nanoparticles formed during the reaction may be aggregated. In this case, it is difficult to uniformly control the particle size of the metal precursor nanoparticles, and a solution containing the metal precursor nanoparticles is formed on the substrate layer It may be difficult to form a uniform and thin coating layer. Further, in order to control the reaction rate of such a highly reactive compound, an expensive microchannel reactor has been used, but a method of controlling the reaction rate at a lower cost is required.
The present application provides a reactor capable of controlling the rate of reaction of highly reactive compounds.
The present application relates to a reactor. According to the exemplary reactor of the present application, the explosion reaction rate of the metal nanoparticle precursor is suppressed by injecting a solution containing the metal precursor into a solution containing a reactive compound having a very high reactivity with the metal precursor, The particle size of the precursor nanoparticles can be controlled to be small, and thus a film having a uniform surface roughness can be produced in a large area.
Hereinafter, a manufacturing method of the present application will be described with reference to the accompanying drawings. The accompanying drawings are merely exemplary and are not intended to limit the method of manufacture of the present application.
BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a diagram exemplarily showing an injection device used in the production method of the present application. Fig.
Exemplary reactors of the present application include a reaction tank and a reaction rate control section.
The reaction tank refers to a water tank or a vessel where the reaction takes place. In one example, the reaction tank may be filled with a solution containing a reactive compound which reacts with the metal precursor.
The metal precursor may include at least one selected from the group consisting of metal nitrate, metal acetate, and metal chloride. The metal is not particularly limited as long as it is a metal capable of reacting with the reactive compound, and may be, for example, a metal of
The reactive compound is a compound having a very high reactivity with the metal precursor. The reaction between the metal precursor and the reactive compound may satisfy the following general formula (1).
[Formula 1]
Rp > 1 [mu] m / min
In the general formula (1), Rp represents the rate of increase of the particle size, which is a reactant of the metal precursor and the reactive compound within Ts time,
And Ts represents the time at which the growth of the particle size is saturated.
2 is a graph exemplarily showing the change in particle size or diameter with the reaction time
For example, as shown in FIG. 2, depending on the reaction time, the particle size may change in the form of a quadratic function. As shown in FIG. 2, the time at which the growth of the particle size is saturated corresponds to the time at which the particle size grows explosively according to the reaction time and the boundary of the region where the growth of the particle size slows according to the reaction time, For example, Ts is the time at the point where the first straight line of the graph during the growth time of the particle size and the first straight line of the graph in the time region in which the growth of the particle is saturated in the graph of Fig. 2 . ≪ / RTI > For example, in the left region of Ts time in Fig. 2, the particle size exponentially grows according to the reaction time, for example, the increase rate of the particle size in the left region of Ts time may be 1 탆 / min or more . 2, the growth of the grain size does not occur or grows at a very low rate depending on the reaction time. For example, the increase rate of the grain size in the right region of the Ts time is 1 탆 / min ≪ / RTI >
In the case where the reaction of the metal precursor with the reactive compound satisfies the general formula 1, that is, in the case where the increase rate of the particle size, which is a reactant of the metal precursor and the reactive compound, is 1 m / min or more within the Ts time, It is possible to control the particle size of the precursor nanoparticles to be small even at a small cost by effectively suppressing the explosion reaction rate of the metal nanoparticle precursor using the reactor of the application, Area can be manufactured.
In one example, the reactive compound may be a compound represented by the following formula (1).
[Chemical Formula 1]
In Formula 1,
M 1 is a Group 1 metal,
R 1 and R 2 each independently represent alkyl having 1 to 12 carbon atoms.
For example, M 1 can be a Group 1 alkali metal, such as lithium, sodium or potassium, and in one example, sodium.
Each of R 1 and R 2 may independently be an alkyl group having 1 to 12 carbon atoms, for example, 1 to 8 carbon atoms, 1 to 6 carbon atoms, or 1 to 4 carbon atoms. For example, R 1 and R 2 may each independently be methyl, ethyl, propyl, butyl, pentyl or hexyl, and in one example may be methyl, but is not limited thereto.
In one example, the compound of Formula 1 may be sodium dimethyldithiocarbamate (CH 3 ) 2 NCSSNa · 2H 2 O, and the solution containing the reactive compound may be sodium dimethyldithiocarbamate Mate. ≪ / RTI >
The first solvent in which the compound of Formula 1 is dissolved is selected from the group consisting of alcohol (C n H 2n + 1 OH, 1? N? 6) -based solvent such as methanol, 2-methoxyethanol, methanol, And may be, for example, methanol, but is not limited thereto.
The reaction rate control unit controls the reaction rate of the metal precursor and the reactive compound in the reaction tank. As described above, when the metal precursor has a very high reaction rate with the reactive compound such as the compound of Formula 1, an explosive reaction occurs when the first solution and the second solution are simply mixed. In this case, it is difficult to control the particle size of the metal precursor nanoparticles evenly, and a solution containing the metal precursor nanoparticles is coated on the substrate layer It may be difficult to form a uniform and thin coating layer. Thus, in the reactor of the present application, the solution containing the metal precursor is injected into the solution containing the reactive compound by the reaction rate control unit and mixed, whereby the metal precursor nano-particles are highly dispersed and precipitated in the mixed solution, Thus, controlled metal precursor nanoparticles can be formed with a controlled average particle size and a particle size distribution (PSD) with very small standard deviation. Further, in the prior art, an expensive microchannel reactor has been used to control the reaction rate of such a highly reactive compound. However, according to the present reactor, by controlling the reaction rate using the injection device, There is an advantage that the speed can be controlled.
In one embodiment, the solution comprising the metal precursor and the solution comprising the reactive compound may be mixed by a spray device, and in one example, a solution comprising the metal precursor is mixed with the reactive compound To prepare a mixed solution.
The first solvent in which the metal precursor is dissolved may be at least one selected from the group consisting of an alcohol (C n H 2n + 1 OH, 1? N? 6) -based solvent such as 2-methoxyethanol, methanol, And can be, for example, methanol, but is not limited thereto.
The spraying apparatus may be an ultrasonic vibration spraying apparatus, an electro spraying apparatus, or a plasma spraying apparatus. For example, the spraying apparatus may be implemented using a spray header or an electric sprayer equipped with an ultrasonic generator . In this case, the injection may be performed to inject at a flow rate of 20 ml / hr or less, for example 15 ml / hr or less or 10 ml / hr or less.
The solution containing the metal precursor and the solution containing the reactive compound may be mixed to prepare a mixed solution. In the mixed solution, a metal precursor in the solution containing the metal precursor and a reactive compound in the solution containing the reactive compound, for example, a compound of the formula 1, are formed to form a metal precursor nanoparticle of the following formula . Accordingly, the mixed solution may include metal precursor nanoparticles of Formula 2, and may further include a first solvent contained in a solution containing the metal precursor and a solution containing a reactive compound.
(2)
In Formula 2, M 2 may be a metal of
Each of R 3 and R 4 may independently be an alkyl group having 1 to 12 carbon atoms, for example, 1 to 8 carbon atoms, 1 to 6 carbon atoms, or 1 to 4 carbon atoms. For example, R 3 and R 4 may each independently be methyl, ethyl, propyl, butyl, pentyl, or hexyl, and in one example may be methyl, but is not limited thereto.
In one example, the compound of
In one example, the average particle size of the metal precursor nanoparticles of
The metal precursor nanoparticles of
Another embodiment of the present application relates to a method for producing a metal nitride film using the metal precursor nanoparticles of formula (2) obtained in the reactor.
In one example, the metal precursor nanoparticles of
After the solution is prepared, a metal precursor nanoparticle solution comprising the metal precursor nanoparticles may be coated on the substrate layer.
The coating can be carried out through various coating methods known in the art, for example, spray coating, spin coating, screen printing or dip coating, but is not limited thereto.
As described above, since the prepared metal precursor nanoparticles have a very small average particle size and a narrow range of particle size distribution, and thus the metal precursor nanoparticles have a uniform and small particle diameter, the coating layer of the metal precursor nanoparticle solution It can have a very thin thickness and a uniform thickness.
The coating layer of the metal precursor nanoparticle solution may be formed to have a thickness of 15 μm or less, and the metal nitride layer formed after the heat treatment to be described later may have a thickness of 10 μm or less.
In the metal precursor nanoparticle solution, the second solvent for dispersing the metal precursor nanoparticles of
The metal precursor nanoparticle solution layer coated on the base layer may be heat-treated in a nitrogen gas or ammonia gas atmosphere, and the sulfur atom of the compound of formula (2) in the metal precursor nanoparticle solution layer by the heat treatment may be nitrogen gas or ammonia Nitrogen atom of the gas. As a result, a film including a metal nitride layer having a thin thickness and a uniform thickness can be finally produced.
Fig. 3 is a diagram exemplarily showing an apparatus in which heat treatment is performed in the manufacturing method of the present application. Fig.
As shown in FIG. 3, the heat treatment may be performed in a furnace. The heating furnace may be maintained in a nitrogen or ammonia gas atmosphere. The heating furnace may comprise a quartz tube, and a supporting means for fixing the base layer may be disposed in the heating furnace.
In one example, the heat treatment may be performed at a temperature of 500 ° C to 1200 ° C, for example, at a temperature of 600 to 1000 ° C or 800 to 900 ° C, but is not limited thereto. In addition, the heat treatment may be performed for 5 minutes to 60 minutes, for example, 10 minutes to 50 minutes, or 15 minutes to 30 minutes, but is not limited thereto.
In one example, the metal nitride layer formed by the heat treatment of the metal precursor nanoparticle solution layer containing the metal precursor nanoparticles of
[Reaction Scheme 1]
2Ga (S 2 CN (CH 3 ) 2 ) 3 → 2Ga 2 S 3 + adducts
[Reaction Scheme 2]
Ga 2 S 3 + 2NH 3 ? 2GAN + 3H 2 S
The present application also relates to a film produced by the above-described production method. Exemplary films of the present application include a very thin and uniform thickness metal nitride layer of several micrometers as produced using the precursor metal precursor nanoparticles obtained by the reactors of the present application, Sulfur atoms in the metal precursor nanoparticles of the metal precursor of the present invention are doped in a part of the metal nitride layer and the sulfur component is detected as a PL spectra on the surface.
Hereinafter, the film of the present application will be described with reference to the accompanying drawings. The accompanying drawings are by way of example and do not limit the film of the present application.
4 is a cross-sectional view schematically showing the film of the present application.
As shown in Fig. 4, the
The metal nitride layer (12) satisfies the following general formula (2) as a spectral luminousness (PL) spectrum measured using a laser having a wavelength of 325 nm.
[Formula 2]
E (I max ) = E g - 0.1 x k
In the
E (I max ) represents the band gap energy at the position having the maximum intensity value of the optical luminescence spectrum,
Eg represents the band gap energy of the metal nitride,
k is a rational number of more than 2 and less than 6.
The term " optical luminescence " refers to a phenomenon in which a material emits light by being stimulated by light, and more specifically, when electrons in a material absorbing light are brought into an excited state and then returned to the original state It means a phenomenon of light emission. The term "photoluminescence (PL) spectrum" refers to a spectrum that irradiates light to a material and exhibits relative intensities representing the distribution of the energy of the light emitted from the material to which the light is irradiated, using optical luminescence , And the intensity of the optical luminescence spectrum has a maximum intensity value (hereinafter referred to as a peak value) in a unique energy band depending on the material. The intensity values of the optical luminescence spectrum are relative values, and thus are expressed in units of a.u (arbitrary unit).
The PL measurement can be performed using a He-Cd laser having a center wavelength of 325 nm as an excitation light source. The measurement temperature is not particularly limited, but it is preferable to perform the measurement at 20 K or less. For example, Omnichrome series 74 He-Cd laser, Acton SpectraPro 2300i spectrometer, Princeton Instruments PI-MAX1024HQ-Blu CCD detector, and the like are examples of devices capable of PL measurement under these conditions. On the other hand, in the PL measurement, there is a case in which the strength of the PL spectrum can not be sufficiently obtained in a crystal having a high carrier concentration in crystals, and evaluation can not be made. In this case, undoped GaN (i-GaN) may be laminated on the crystal surface of the object to be measured by MOCVD or the like to reduce the influence of the carrier during the low-temperature PL measurement, and then measurement can be performed. The thickness of the i-GaN layer to be laminated may be usually 0.01 占 퐉 or more, for example, 0.1 占 퐉 or more, or 0.5 占 퐉 or more. Further, the thickness of the i-GaN layer may be generally 100 mu m or less, for example, 10 mu m or less, or 5 mu m or less. If the thickness of the i-GaN layer to be laminated is too thin, the influence of the carrier can not be sufficiently reduced. If it is too large, the influence of defects occurring in the stacked i-GaN layer can be detected.
The
In one example, when the metal nitride layer is a gallium nitride layer, the metal nitride layer satisfying the
For example, in the case of the gallium nitride layer, as shown in Fig. 7, the band gap energy at the position having the maximum intensity value of the luminousness spectrum represented by the sulfur component is 2.95 eV, and the band gap energy of gallium nitride is 3.44 eV , The k value calculated according to the general formula (2) is 4.9, thereby satisfying the general formula (2).
The sulfur component detected on the surface of the
The "XPS analysis" is a method of using X-rays as a light source in the electro-spectroscopy. When X-rays are irradiated onto a substance, the photoelectrons are emitted to the outside of the substance. And therefore, it means a method of examining the atomic composition of the substance and the bonding state of the electrons.
As described above, the
In the above, the centerline average roughness is obtained by extracting the center line average roughness by a reference length L in the direction of the average line in the roughness curve, calculating the roughness curve as a function y = f (x ) Denotes a value which can be obtained by the following formula (1) in terms of micrometers (占 퐉). The center line average roughness is measured under the standards of JIS B0031, JIS B0601 or ISO 468.
[Equation 1]
In one example, the metal may be at least one selected from the group consisting of gallium, aluminum, indium, and lead, and may be, for example, gallium, but is not limited thereto.
The
As described above, the
In one example, the
According to the reactor of the present application, the explosion reaction rate of the metal nanoparticle precursor is suppressed by injecting a solution containing the metal precursor into a solution containing a reactive compound having a very high reactivity with the metal precursor, The particle size of the particles can be controlled to be small, and thus a film having a uniform surface roughness can be produced in a large area.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a view showing an exemplary reactor of the present application. FIG.
FIG. 2 is a graph showing changes in particle size with respect to reaction time. FIG.
Fig. 3 is an exemplary view showing an apparatus in which the heat treatment is performed in the method of the present application. Fig.
4 is a cross-sectional view schematically showing the film of the present application.
5 (a) is a 1 H-NMR spectrum of Ga (DmDTC) 3 nanoparticles, and FIG. 5 (b) is a graph and a photograph showing the size distribution and shape of Ga (DmDTC) 3 nanoparticles.
6 (a) is an XRD pattern of a gallium nitride layer due to thermal decomposition deformation of a Ga (DmDTC) 3 film in an environment where ammonia flows, and FIG. 6 (b) is a SEM photograph of a surface and a cross section of a gallium nitride layer .
Figure 7 shows high resolution XP spectra of
8 shows the PL spectrum of the gallium nitride layer at room temperature.
FIG. 9 shows an XRD pattern and an SEM photograph of an epitaxial gallium nitride film grown on a gallium nitride layer pyrolyzed by MOCVD.
10 is an image of a gallium nitride thin film prepared in Comparative Example using a scanning electron microscope (SEM).
Hereinafter, the present invention will be described in more detail with reference to Examples and Comparative Examples. However, the scope of the present application is not limited by the following description.
The physical properties in the following Examples and Comparative Examples were measured by the following methods and apparatuses.
The synthesized metal precursor Identification of nanoparticles
The metal precursors synthesized in the following Examples and Comparative Examples The nanoparticles were confirmed by 1 H-Fourier transform magnetic resonance system ( 1 H-FT-NMR, Bruker DPX300).
The synthesized metal precursor Measure the size of nanoparticles
The metal precursors synthesized in the following Examples and Comparative Examples The size of the nanoparticles was measured using a particle size analyzer (Beckman Coulter, Inc.) as well as a transmission electron microscope (TEM, Hitachi, H-7600) and X-ray diffraction (XRD, PANalytical, X'pert PRO) N5).
Measurement of structure and morphological properties of metal nitride layers
Structural and morphological properties of the metal nitride layer formed in the following examples and comparative examples were measured using a scanning electron microscope (SEM, Hitachi, S-4100).
Measurement of optoelectronic properties of metal nitride layers
The photoelectric properties of the metal nitride layers formed in the following Examples and Comparative Examples were measured by photoluminescence spectroscopy (PL) using a He-Cd laser at a wavelength of 325 nm.
Measurement of the compositional ratio and bonding of the metal nitride layer
The compositional ratio and bonding of the metal nitride layers formed in the following examples and comparative examples were measured by X-ray photoemission spectroscopy (XPS, VG Microtech, MT 500/1).
Measurement of center line average roughness of metal nitride layer
The centerline average roughness of the metal nitride layer formed in the following examples and comparative examples was calculated by using the formula (1) based on the height data obtained at this time by using AFM (atomic force microscope).
Example 1
A gallium nitride layer was formed on the alumina base layer in the following manner.
(N, N-dimethyldithiocarbamate) -gallium (III) (Ga (S 2 CN (CH 3 ) 2 ) 3 and Ga (DmDTC) 3 ) as a precursor of the gallium nitride layer, The nanoparticles were synthesized by ultrasonic injection.
(Ga (NO 3 ) .8H 2 O) in 50 ml of methanol and 20 ml of sodium dimethyldithiocarbamate ((CH 3 ) 2 ) in methanol to make the molar ratio of the gallium salt and sodium salt to 1.3. 2 NCSSN a. 2H 2 O) were separately prepared.
The gallium nitrate solution was ultrasonically jetted onto the sodium dimethyldithiocarbamate ligand solution at room temperature for 30 minutes and the flow rate of the gallium nitrate solution during the injection process was maintained at 10 ml / hr. The Ga (DmDTC) 3 nanoparticles were synthesized by a very slow precipitation process and the precipitated material was filtered using a centrifugation process. The synthesized Ga (DmDTC) 3 nanoparticles were washed several times with deionized water and dried in a vacuum oven at 60 ° C. for 4 hours. Average particle diameter of the produced Ga (DmDTC) 3 nanoparticles was measured as 28.5 nm, the standard deviation of the particle size distribution of the produced Ga (DmDTC) 3 nanoparticles was measured to be 13.3 nm. The Ga (DmDTC) 3 nanoparticles were dispersed ultrasonically in chloroform (CHCl 3 ) solvent at room temperature for 1 hour.
The solution in which the Ga (DmDTC) 3 nanoparticles were dispersed was spin-coated on a c-axis alumina substrate (1 cm x 1 cm) at 2000 rpm for 30 seconds, dried at room temperature for 10 minutes, Thereby forming a film having a thickness of Ga (DmDTC) 3 5 탆. Thereafter, using the apparatus shown in Fig. 2, Ga (DmDTC) 3 The film was heat-treated at 850 ° C for 10 minutes under an ammonia (NH 3 ) atmosphere at a flow rate of 170 sccm. After the pyrolysis process, the sample was cooled to room temperature under a nitrogen atmosphere to obtain a gallium nitride To form a layered film. In this case, the center line surface roughness of the gallium nitride layer was measured at 7 nm.
Thereafter, a gallium nitride film was epitaxially grown on the produced gallium nitride layer by MOCVD. At this time, the deposition time was maintained at 5 minutes to test the initial growth of the gallium nitride film, and the thickness of the deposited epitaxial gallium nitride film was 500 nm.
Example 2
A film in which an aluminum nitride layer having a thickness of 5 탆 was formed on the alumina base layer was prepared in the same manner as in Example 1, except that aluminum nitrate was used as the metal precursor. In this case, the centerline surface roughness of the aluminum nitride layer was measured to be 7 nm.
In this case, the average particle diameter of the produced Al (DmDTC) 3 nanoparticles was measured as 20 nm, the standard deviation of the particle size distribution of the produced Al (DmDTC) 3 nanoparticles was measured to be 5 nm.
Example 3
A film in which an indium nitride layer having a thickness of 5 占 퐉 was formed on the alumina base layer was prepared in the same manner as in Example 1, except that indium nitrate was used as the metal precursor.
The standard deviation in this case, the average particle size of the prepared In (DmDTC) 3 nanoparticles was measured as 30 nm, prepared In (DmDTC) of 3 nanoparticle particle size distribution is measured by 3 nm. The surface roughness of the center line of the indium nitride layer was measured to be 9 nm.
Example 4
A film in which an indium nitride layer having a thickness of 5 탆 was formed on the alumina base layer was prepared in the same manner as in Example except that indium chloride was used as the metal precursor.
In this case, the average particle size of the prepared In (DmDTC) 3 nanoparticles was measured as 35 nm, the standard deviation of the particle size distribution of the produced In (DmDTC) 3 nanoparticles was measured to be 5 nm. The center line surface roughness of the indium nitride layer was measured to be 10 nm.
Comparative Example
Ga (DmDTC) 3 nanoparticles were formed in the same manner as in Example 1, except that the gallium nitrate solution was not mixed with the sodium dimethyldithiocarbamate ligand solution by ultrasonic irradiation but simply mixed, and the formed nanoparticles were used To prepare a gallium nitride thin film. 10 is an image of a gallium nitride thin film prepared in Comparative Example using a scanning electron microscope (SEM). As shown in FIG. 10, the gallium nitride thin film produced was unable to form a continuous thin film, and it was very difficult to form the thin film with a thickness of 5 μm, and showed a very uneven and irregular porous structure. Accordingly, the surface roughness of the gallium nitride thin film could not be calculated according to the above equation (1).
The average particle diameter of the Ga (DmDTC) 3 nanoparticles prepared above was about 0.1 to 0.5 μm, and the standard deviation of particle diameter of the formed nanoparticles was about 0.1 μm.
5 (a) shows the 1 H-NMR spectrum of Ga (DmDTC) 3 nanoparticles. The spectra represent four peaks of 0 ppm, 1.55 ppm, 3.40 ppm and 7.26 ppm assigned to tetramethylsilane (TMS), water in CDCl 3 , Ga (DmDTC) 3 and CHCl 3 in CDCl 3 , respectively . The tetramethylsilane was used as an internal reference for chemical shift calibration and the peak of the single line at 3.40 ppm is closely related to the chemical shift of the Ga (DmDTC) 3 material. 5 (b) is a graph and a photograph showing the size distribution and shape of Ga (DmDTC) 3 nanoparticles. 5 (b), the Ga (DmDTC) 3 nanoparticles synthesized by the ultrasonic jetting method are well mono-dispersed so as to have an average particle size of 28.5 nm and a standard deviation of 13.3 nm Respectively. In general, the precipitation reaction of gallium nitrate (Ga (NO 3 ) · 8H 2 O) and sodium dimethyldithiocarbamate ((CH 3 ) 2 NCSSNA · 2H 2 O) takes place very quickly, This is relatively difficult. On the other hand, the ultrasonic jetting method is a useful method for controlling the reaction rate, because the size of a plurality of gallium precursor particles in the droplet jetted by ultrasonic waves is relatively small. Therefore, the abrupt reaction of forming large particles was effectively prevented, and the Ga (DmDTC) 3 nanoparticles were easily dispersed in the chloroform solvent.
6 (a) shows an XRD pattern of a GaN layer by thermal decomposition of a Ga (DmDTC) 3 film in an environment where ammonia flows. The XRD peak of the gallium nitride layer is observed mainly at 34.6 degrees and 73.1
[Reaction Scheme 1]
2Ga (S 2 CN (CH 3 ) 2 ) 3 → 2Ga 2 S 3 + adducts
[Reaction Scheme 2]
Ga 2 S 3 + 2NH 3 ? 2GAN + 3H 2 S
The reason that the pyrolyzed gallium nitride layer is well arranged in the (0002) preferential culture direction was expected from the recrystallization process during the pyrolysis reaction. As shown in the
7 is
8 shows the PL spectrum of the gallium nitride layer at room temperature. Three distinct peaks were observed mainly at 3.44 eV, 2.95 eV and 2.69 eV, respectively. The peak at 3.44 eV is assigned to the band edge transition of gallium nitride. Blue luminescence (BL), concentrated at 2.95 eV, was stronger than the other two peaks, indicating the formation of a shallow donor level due to sulfur (S) on the nitrogen (N) site of the gallium nitride layer . ≪ / RTI > As described above in the XPS results, a small amount of sulfur (S) remains in the gallium nitride in the pyrolysis process, and the shallow donor level can be formed due to the substitution of sulfur (S) in the nitrogen (N) have. Generally,
FIG. 9 shows an XRD pattern and an SEM photograph of an epitaxial gallium nitride film grown on a gallium nitride layer pyrolyzed by MOCVD. The epitaxial growth of gallium nitride proceeds in accordance with the following
[Reaction Scheme 3]
Ga (CH 3) 3 (g ) + HCl (g) → GaCl (g) + CH x group (g)
[Reaction Scheme 4]
GaCl (g) + NH 3 ( g) → GaN (s) + HCl (g) + H 2 (g)
The epitaxial gallium nitride film on the pyrolyzed gallium nitride layer exhibited a strong preferential orientation in the (0002) direction due to the hexagonal Wurtzite structure. In addition, the grown gallium nitride film showed lateral growth on the substrate, but the gallium nitride film on the bare sapphire substrate grew upward in the z-axis direction. From this it can be seen that the adsorbed atoms are strongly mixed due to the single-epitaxial properties between the pyrolyzed gallium nitride layer and the grown gallium nitride.
10: Film
11: substrate layer
12: metal nitride layer
Claims (7)
Wherein the reaction rate control unit is a spraying device in which a solution containing a metal precursor is sprayed at a flow rate of 20 ml / hr or less,
Wherein the reaction between the metal precursor and the reactive compound satisfies the following general formula 1:
[Formula 1]
Rp? 1 占 퐉 / min
In the general formula (1), Rp represents the rate of increase of the particle size, which is a reactant of the metal precursor and the reactive compound within Ts time,
And Ts represents the time at which the growth of the particle size is saturated.
[Chemical Formula 1]
In Formula 1,
M 1 is a Group 1 metal,
R 1 and R 2 each independently represent alkyl having 1 to 12 carbon atoms.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020160016377A KR101840534B1 (en) | 2016-02-12 | 2016-02-12 | Reactor |
PCT/KR2016/015034 WO2017138695A1 (en) | 2016-02-12 | 2016-12-21 | Reactor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020160016377A KR101840534B1 (en) | 2016-02-12 | 2016-02-12 | Reactor |
Publications (2)
Publication Number | Publication Date |
---|---|
KR20170094979A KR20170094979A (en) | 2017-08-22 |
KR101840534B1 true KR101840534B1 (en) | 2018-05-04 |
Family
ID=59563686
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020160016377A KR101840534B1 (en) | 2016-02-12 | 2016-02-12 | Reactor |
Country Status (2)
Country | Link |
---|---|
KR (1) | KR101840534B1 (en) |
WO (1) | WO2017138695A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110976845A (en) * | 2019-12-04 | 2020-04-10 | 华南理工大学 | Powder modification method for eliminating thermal cracks of 7075 aluminum alloy formed by laser 3D printing |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001198450A (en) | 2000-01-19 | 2001-07-24 | Komatsu Ltd | Hydrothermal reactor |
WO2008127425A2 (en) | 2006-11-22 | 2008-10-23 | S.O.I.Tec Silicon On Insulator Technologies | Abatement of reaction gases from gallium nitride deposition |
KR100892753B1 (en) | 2007-10-10 | 2009-04-15 | 세메스 주식회사 | Apparatus and method for preparing catalyst for systhesis of carbon-nano-tube |
US20100016148A1 (en) | 2007-12-24 | 2010-01-21 | Joung Hyeon Lim | Process for preparing catalyst for synthesis of carbon nanotubes using spray pyrolysis |
US20100272617A1 (en) | 1999-11-01 | 2010-10-28 | Moore Robert R | Falling film plasma reactor |
KR101499565B1 (en) * | 2014-04-17 | 2015-03-10 | 주식회사 라이트브릿지 | Apparatus and method for manufacturing metal nanoparticles using plasma |
JP2016168585A (en) | 2015-03-12 | 2016-09-23 | 株式会社リコー | Fluid treatment apparatus |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100396721B1 (en) * | 2001-09-18 | 2003-09-02 | 율촌화학 주식회사 | Methods for Preparation of Nano-Sized Metal Colloid |
KR101465324B1 (en) * | 2013-04-04 | 2014-11-28 | 성균관대학교산학협력단 | Method of manufacturing copper-gallium nano-particles using ultrasound and method of manufacturing copper-indium-gallium nano-particles using the copper-gallium nano-particles |
KR101508281B1 (en) * | 2013-12-06 | 2015-07-09 | 한화케미칼 주식회사 | Method for preparation of uniform metal oxide nanoparticles with high reproducibility |
-
2016
- 2016-02-12 KR KR1020160016377A patent/KR101840534B1/en not_active Application Discontinuation
- 2016-12-21 WO PCT/KR2016/015034 patent/WO2017138695A1/en active Application Filing
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20100272617A1 (en) | 1999-11-01 | 2010-10-28 | Moore Robert R | Falling film plasma reactor |
JP2001198450A (en) | 2000-01-19 | 2001-07-24 | Komatsu Ltd | Hydrothermal reactor |
WO2008127425A2 (en) | 2006-11-22 | 2008-10-23 | S.O.I.Tec Silicon On Insulator Technologies | Abatement of reaction gases from gallium nitride deposition |
KR100892753B1 (en) | 2007-10-10 | 2009-04-15 | 세메스 주식회사 | Apparatus and method for preparing catalyst for systhesis of carbon-nano-tube |
US20100016148A1 (en) | 2007-12-24 | 2010-01-21 | Joung Hyeon Lim | Process for preparing catalyst for synthesis of carbon nanotubes using spray pyrolysis |
KR101499565B1 (en) * | 2014-04-17 | 2015-03-10 | 주식회사 라이트브릿지 | Apparatus and method for manufacturing metal nanoparticles using plasma |
JP2016168585A (en) | 2015-03-12 | 2016-09-23 | 株式会社リコー | Fluid treatment apparatus |
Also Published As
Publication number | Publication date |
---|---|
WO2017138695A1 (en) | 2017-08-17 |
KR20170094979A (en) | 2017-08-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Zhang et al. | Growth and luminescence of zinc-blende-structured ZnSe nanowires by metal-organic chemical vapor deposition | |
US8410470B2 (en) | Core-shell quantum dot fluorescent fine particles | |
JP2012169622A (en) | Method and system for forming thin film | |
Hsu et al. | Vertical single-crystal ZnO nanowires grown on ZnO: Ga/glass templates | |
Deo et al. | Metal chalcogenide nanocrystalline solid thin films | |
Kamruzzaman et al. | Effect of temperature, time, concentration, annealing, and substrates on ZnO nanorod arrays growth by hydrothermal process on hot plate | |
KR101840534B1 (en) | Reactor | |
Li et al. | Nanoscale semiconductor–insulator–metal core/shell heterostructures: facile synthesis and light emission | |
KR101851842B1 (en) | Film, manufacturing metohd of the film and light emitting diode comprising thereof | |
US7772288B2 (en) | Group III nitride coatings and methods | |
CN101068890B (en) | Group III nitride coatings and methods | |
Ji et al. | Deposition and characteristics of PbS thin films by an in-situ solution chemical reaction process | |
Achary et al. | One-step growth of isolated CdO nanoparticles on r-sapphire substrates by using the spray pyrolysis methodology | |
Prabhakar et al. | Ultra-thin conformal deposition of CuInS 2 on ZnO nanowires by chemical spray pyrolysis | |
Abdallah et al. | Synthesis of PbS: ZnO nanotrees by thermal evaporation: morphological, structural and optical properties | |
Umar et al. | Synthesis of ZnO nanowires on steel alloy substrate by thermal evaporation: Growth mechanism and structural and optical properties | |
Rizal et al. | Gallium phosphide nanowires for optoelectronic devices | |
Black et al. | The optical properties of vertically aligned ZnO nanowires deposited using a dimethylzinc adduct | |
JP2020147464A (en) | Manufacturing method of metal nitride film | |
Yahiaoui et al. | Photoluminescence studies and crystal field calculations of Yb-doped InGaN nanorods | |
Yong et al. | Sol-Gel Spin Coating Growth Of Gallium Nitride Thin Films A Simple, Safe, and Cheap Approach (Penerbit USM) | |
Li et al. | Construction, characterization, and growth mechanism of high-density jellyfish-like GaN/SiO x N y nanomaterials on p-Si substrate by Au-assisted chemical vapor deposition approach | |
Jin et al. | Preparation, structure, and photoluminescence properties of Ga2O3/SnO2 coaxial nanowires | |
Lee et al. | Structure and luminescence of CdO-coated ZnSe nanorods | |
PL237260B1 (en) | Method for producing quantum nanostructures/heterostructures and three-component ZnMgO compounds on substrates that contain the nanostructures |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A201 | Request for examination | ||
E902 | Notification of reason for refusal |