WO2020054974A1 - Sublimation purification apparatus and sublimation purification method - Google Patents

Sublimation purification apparatus and sublimation purification method Download PDF

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Publication number
WO2020054974A1
WO2020054974A1 PCT/KR2019/009812 KR2019009812W WO2020054974A1 WO 2020054974 A1 WO2020054974 A1 WO 2020054974A1 KR 2019009812 W KR2019009812 W KR 2019009812W WO 2020054974 A1 WO2020054974 A1 WO 2020054974A1
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WO
WIPO (PCT)
Prior art keywords
boat
sublimation purification
chamber
tube housing
heating zone
Prior art date
Application number
PCT/KR2019/009812
Other languages
French (fr)
Korean (ko)
Inventor
홍석광
김형석
이헌영
정광진
신영환
Original Assignee
주식회사 엘지화학
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from KR1020190066109A external-priority patent/KR102297249B1/en
Application filed by 주식회사 엘지화학 filed Critical 주식회사 엘지화학
Priority to JP2020539202A priority Critical patent/JP7052172B2/en
Priority to US16/968,365 priority patent/US11426678B2/en
Priority to EP19858777.6A priority patent/EP3734683B1/en
Priority to CN201980012120.4A priority patent/CN111699565B/en
Publication of WO2020054974A1 publication Critical patent/WO2020054974A1/en

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    • HELECTRICITY
    • H10SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
    • H10KORGANIC ELECTRIC SOLID-STATE DEVICES
    • H10K71/00Manufacture or treatment specially adapted for the organic devices covered by this subclass

Definitions

  • the present invention relates to a sublimation purification apparatus and a sublimation purification method, and more particularly, to a sublimation purification apparatus and a sublimation purification method capable of realizing a high-purity purification efficiency and improving yield due to a continuous process and reducing production time.
  • the electroluminescent device is a self-luminous device that emits phosphors by recombination of electrons and holes, and may have a purity of a light-emitting layer material as a factor affecting the luminescence properties of the electroluminescent device.
  • organic electroluminescent device organic The purity of the material greatly affects the luminescence properties of the device.
  • impurities are mixed in the organic material, it is necessary to purify the organic material in order to remove these impurities because the impurities become a trap of carriers or cause quenching, which significantly decreases the luminous intensity and luminous efficiency of the device. have.
  • a recrystallization method using a solvent or recrystallization using a solvent is generally used. Since the recrystallization method by sublimation has an organic substance sublimation and recrystallization under vacuum, it has a property that impurities do not enter, and thus, a conventional train-sublimation method may be used for purification of an organic material for an organic EL device.
  • the first heating zone (1) by heating and vaporizing the organic material (6) containing the purified material and impurities, the gases through the quartz tube (5) Molecular movement is performed in the direction of pumping, and at this time, the phase changes while liquefying or solidifying while meeting the second heating zone 2 and the third heating zone 3 having different temperature regions, thereby purifying the purified material 7 and impurities 8 It can be collected separately.
  • the conventional sublimation purification apparatus is provided with several second quartz tubes 20 inside the first quartz tube 10 for vacuum, but outside the first quartz tube 10 It can be made by installing a heater cover 30 is provided with a ceramic heater (31). When the organic material 51 is introduced into the sublimation purification device, and the heater cover 30 is closed and the ceramic heater 31 is heated, the purification material 52 and impurities 53 due to the temperature gradient inside the sublimation device Separation is achieved.
  • the first quartz tube 10 is used for airtightness with a vacuum atmosphere or the atmosphere, and the second quartz tube 20 is separated into a plurality of sections and controlled at different temperatures to control the organic material 51.
  • Purification material 52 is obtained by removing impurities.
  • the internal material of the sublimation purification device has the disadvantage that the yield is lowered and the manpower is increased due to the limitations of mass production due to the disadvantages of the material and the difficulty of having the process continuity.
  • the problem to be solved by the present invention is to improve the process continuous automation through metallization of the internal material, high purity purification efficiency, yield improvement due to the continuous process, and metallization of the internal material to compensate for the limitations of the design process limitation and the durability of the quartz, which is the material of the refiner, and It is to provide a sublimation purification apparatus and a sublimation purification method that realizes a reduction in production time and the like.
  • An apparatus for sublimation purification includes a vacuum chamber, a tube housing positioned in the vacuum chamber, a boat in close contact with the tube housing, and a heating positioned adjacent to the outer surface of the tube and the outer surface of the tube housing It includes a portion, and the sublimation target material is contained in the boat, and at least one of the boat and the tube housing is formed of metal.
  • the boat includes a first boat and a second boat, and the first boat and the second boat are located together in the vacuum chamber, and the tube housing becomes a movement path, whereby the sublimation purification material contained in the first boat is After being heated, it can be allowed to be captured in the second boat.
  • the heating unit located adjacent to the outer surface of the tube housing is a first heating zone located in a portion corresponding to the first boat, a second heating zone located between the first boat and the second boat, and the second boat It includes a third heating zone located in the portion corresponding to, the first heating zone is the sublimation purification target material activated by the gas contained in the first boat to control the temperature to maintain the gas state, the second heating The zone is to sublimate the substance to be purified sublimation activated by the gas, and the third heating zone is to control the temperature to maintain the solution status of the substance to be sublimated purification to sublimate purification in the solution state to the second boat. You can make the target material fall.
  • the tube housing may have a tilted structure along the movement path of the sublimation purification target material.
  • the metal may include titanium or tantalum.
  • the sublimation purification device further includes a sealing gasket formed at an end of the tube housing, and the sealing gasket may be interposed between the tube housing and the boat.
  • the sealing gasket may include at least one of titanium (Ti), silver (Ag), copper (Cu), and ceramic.
  • the sublimation purification apparatus includes a chamber moving part, a plurality of chambers located adjacent to the chamber moving part, a tube housing located in the chamber, and located between the chamber moving part and the chambers A gate, a boat moving inside the chamber moving part by a transfer robot or loading or unloading from the chamber moving part into the chamber, and a heating part surrounding the outer surface of the boat and the outer surface of the tube housing,
  • the boat includes a first boat and a second boat connected to each other with the tube housing.
  • the heating unit located adjacent to the outer surface of the tube housing is a first heating zone located in a portion corresponding to the first boat, a second heating zone located between the first boat and the second boat, and the second boat It includes a third heating zone located in the portion corresponding to, the first heating zone is the sublimation purification target material activated by the gas contained in the first boat to control the temperature to maintain the gas state, the second heating The zone is to sublimate the substance to be purified sublimation activated by the gas, and the third heating zone is to control the temperature to maintain the solution status of the substance to be sublimated purification to sublimate purification in the solution state to the second boat. You can make the target material fall.
  • the tube housing may have a tilted structure along the movement path of the sublimation purification target material.
  • the sublimation purification device may further include an up-and-down transfer device that moves at least one of the first and second boats to the tube housing by moving the boat passing through the gate in the chamber.
  • At least one of the boat and the tube housing may be formed of metal.
  • the sublimation purification apparatus further includes a sealing gasket formed at an end of the tube housing, and when the boat is loaded into the chamber and engaged with the tube housing, the sealing gasket is interposed between the tube and the tube housing. You can.
  • the plurality of chambers includes a first chamber and a second chamber adjacent to each other, and the tube housing positioned in the first chamber is removed by heating a sublimation purification target material contained in the first boat loaded in the first chamber Sublimation purification targets contained in the first boat loaded into the second chamber, where impurities are captured in the second boat, the first boat unloaded from the first chamber is loaded into the second chamber through the chamber moving part, and The material can be melted and activated with gas.
  • the sublimation purification device may further include a sublimation purification amount measurement member fixed inside the chamber, and the sublimation purification amount measurement member may be located below the boat.
  • the sublimation purification device may further include an up-and-down transfer device that moves at least one of the first and second boats to the tube housing by moving the boat passing through the gate in the chamber.
  • the boat may be spaced apart from the tube housing by the transfer device to reach the sublimation purification amount measurement member to measure the sublimation purification amount.
  • the sublimation purification method comprises loading a first boat containing a sublimation purification target material in a first chamber, and impurities removed by heating the sublimation purification target material contained in the loaded first boat Capturing to the second boat through the tube housing, unloading the first boat from the first chamber and loading the first boat into the second chamber through a transfer robot, loaded into the second chamber Melting the sublimation purification target material contained in the first boat and activating it with gas, liquefying the gas-activated material, and transporting the solution through the tube housing included in the second chamber; Capturing to a second boat located in the second chamber, the second boat located in the second chamber to the cooling chamber using the transfer robot And cooling the liquefied material contained in the second boat loaded in the cooling chamber, wherein at least one of the first boat, the second boat and the tube housing is formed of metal.
  • the sublimation purification method may further include cleaning a chemical solution of parts formed of a metal in the first boat, the second boat, and the tube housing.
  • the sublimation purification method may further include baking after the washing step.
  • the material for an organic light emitting device according to another embodiment of the present invention is purified by the sublimation purification method described above.
  • the organic light emitting device includes a material for an organic light emitting device described above.
  • 1 shows a principle diagram of purification of an organic material.
  • FIG. 2 is a cross-sectional view showing a conventional purification device.
  • Figure 3 is a schematic diagram showing a sublimation purification apparatus according to an embodiment of the present invention.
  • FIG. 4 is an enlarged view showing a form in which the tube housing and the boat located in one chamber are closely attached in the sublimation purification apparatus of FIG. 3.
  • FIG. 5 is a view showing a modified embodiment in which a part of the tube housing has a tilted structure in the sublimation purification device of FIG. 4.
  • FIG. 6 is a view showing a state in which the boat is loaded into the chamber in the sublimation purification apparatus of FIG. 3.
  • FIG. 7 is a perspective view showing a state in which the tube housing and the boat are in close contact in FIG. 4.
  • FIG. 8 is a perspective view showing a heating unit according to an embodiment of the present invention.
  • FIG. 9 is a view showing a state in which the boat is in close contact with the tube housing in one chamber of the sublimation purification apparatus according to another embodiment of the present invention.
  • FIG. 10 is a perspective view showing a vertical transfer device and a sublimation purification amount measuring member in part A of FIG. 9.
  • FIG. 11 is a front view showing the sublimation purification amount measuring member of FIG. 10.
  • planar this means when the object portion is viewed from above, and when it is referred to as “cross-sectional”, it means when the cross section of the object portion vertically cut is viewed from the side.
  • Figure 3 is a schematic diagram showing a sublimation purification apparatus according to an embodiment of the present invention.
  • the sublimation purification apparatus 1000 includes a chamber moving part 600, a plurality of chambers 110, 120, 130, 140, and a chamber moving part 600 and chambers 110, 120 , 130, 140.
  • the tube housing 200 is located in each chamber 110, 120, 130, 140, and two boats 300 can be connected to each other by the tube housing 200.
  • the bow 300 may be in close contact with the tube housing 200 to perform a sublimation purification process.
  • Each of the plurality of chambers 110, 120, 130, and 140 may be a vacuum chamber. It is preferable that the chamber moving part 600 also maintains a vacuum state.
  • the sublimation purification apparatus 1000 includes a heating unit 400 and a cooling unit covering the heating unit 400 located adjacent to the outer surface of the tube housing 200 located inside the chambers 110, 120, 130, and 140. 500.
  • the heating part 400 is also formed in a portion adjacent to the outer surface of the boat 300.
  • the sublimation purification apparatus 1000 further includes a cooling chamber 150 in addition to the plurality of chambers 110, 120, 130 and 140 in order to recover the material for the organic light emitting device in the final step of the sublimation purification process It can contain. Inside the cooling chamber 150, there is no tube housing 200 located inside the other chambers 110, 120, 130, 140, and only the cooling unit 500 may be included. Cooling chamber 150, after the purification process, when the boat 300 containing the material purified by the transfer robot 650 passes through the gate 700 and is loaded into the cooling chamber 150, the purified material in solution state After cooling, the material for an organic light emitting device for use as a product can be recovered.
  • the transfer robot 650 is located in the chamber moving unit 600, and the bow 300 moves the inside of the chamber moving unit 600 by the transfer robot 650 or the chambers 110 and 120 are moved in the chamber moving unit 600. , 130, 140, 150).
  • the bow 300 is loaded or unloaded from the chamber moving part 600 to each chamber 110, 120, 130, 140, 150, the chamber moving part 600 and each chamber 110, 120, 130, 140 , 150, the boat 300 positioned between the gates 300 may pass through.
  • the boat 300 loaded through the gate 700 and loaded inside the chambers 110, 120, 130, and 140 may be in close contact with the tube housing 200 by the vertical transfer device 800.
  • At least one of the boat 300 and the tube housing 200 according to the present embodiment may be formed of metal.
  • the bow 300 and the tube housing 200 are parts made of the inner material of the sublimation purification apparatus 1000, and the part made of the inner material is a part of the bow 300 and the tube housing 200 that comes into contact with the substance to be purified.
  • the metal may include titanium, tantalum, alumina, stainless steel, tungsten, silver, copper, invar, aluminum, and the like. It may be preferably titanium or tantalum. Quartz, which has been used in the related art, is a kind of general glass, and is made of only silicon dioxide, which is a main component, and has a very low impurity content, and is used for semiconductors, laboratory equipment, and optical components.
  • Quartz has advantages in that it has a material of light transmittance, thermal stability, chemical resistance and high purity, but it is vulnerable to durability, has limitations in processing parts, and has a disadvantage of low thermal conductivity. Therefore, if a sublimation purification device is manufactured of quartz material, there is a limitation in size processing, and if the size of the thickness is large due to low thermal conductivity, it takes a long time to heat the sublimation purification, and the irrationality of work during disassembly / assembly It is difficult to mass-produce purified substances due to the like.
  • titanium can be used, and titanium is light and hard with a small specific gravity of the metal, and is excellent in corrosion resistance and excellent in deformation and corrosion. Therefore, it is possible to effectively control the phase change of a material to be melted using a high-strength material component, and there is little limitation in size processing.
  • tantalum can be used, and tantalum is excellent in ductility, easy to process, and has very good thermal conductivity and electrical conductivity.
  • titanium can also be used, and since titanium has the characteristics described above, it is easy to clean and heat transfer is stable, so it is easy to change the phase by accurately controlling the heating conditions, and each phase-changed material It may be easy to move between the chambers corresponding to the purification zone.
  • tantalum can also be used as an example of the metallic material of the tube housing.
  • outgassing and other impurities mixed in a substance to be sublimated contained in the boat 300 are removed.
  • the process can be performed.
  • the outgassing and other impurities may be organic impurities mixed in a sublimation purification target material.
  • Outgassing is a solvent used in a synthesis process, which is a step prior to the sublimation process, and is a solvent such as ethanol, water, and hexane, and other impurities may be monomolecular compounds smaller than a good molecular weight.
  • the first chamber 110 and the third chamber 130 shown in FIG. 3 contain the substance to be sublimed in the left side 300, and the right side 300 after heating in the tube housing 200. Cooled outgassing and other impurities are captured. Therefore, the primary sublimation purified material remains on the left side of the boat 300, and the primary sublimation purified material containing the boat 300 can be moved to the second chamber 120 and the fourth chamber 140. .
  • the first sublimation purified material is contained in the bow 300 of each of the second chamber 120 and the fourth chamber 140, and the material is melted and gasified while passing through the heating unit 400,
  • the liquefied material is liquefied, and the liquefied material can be captured as a sublimation purified material on the right side boat 300.
  • Sublimation purified material captured on the right boat 300 of the second chamber 120 and the fourth chamber 140 may be transferred to the cooling chamber 150 to be recovered as a material for an organic light emitting device through a cooling process.
  • the tube housing 200 located in the first chamber 110 heats the sublimation purification material contained in the first boat loaded in the first chamber 110 to remove impurities removed from the second boat.
  • the first boat unloaded from the first chamber 110 is loaded into the second chamber 120 through the chamber moving part 600, and the sublimation purification target contained in the first boat loaded in the second chamber 120
  • the material is melted and activated with gas, the gasified material is in solution, and the solution can be captured as a sublimated purified material in the second boat.
  • the right boat 300 of the second chamber 120 is directly moved to the cooling chamber 150, or additional sublimation
  • the purification process sequentially performed in the first chamber 110 and the second chamber 120 may be repeated once again in the third chamber 130 and the fourth chamber 140.
  • the tube housing 200, the boat 300, the heating unit 400, and the cooling unit associated with the sublimation purification path are located inside each chamber 110, 120, 130, and 140. (500) will be described in detail.
  • FIG. 4 is an enlarged view of a tube housing and a boat positioned in one chamber in a sublimation purification apparatus of FIG. 3 in close contact.
  • FIG. 5 is a view showing a modified embodiment in which a part of the tube housing has a tilted structure in the sublimation purification device of FIG. 4.
  • FIG. 6 is a view showing a state in which the boat is loaded into the chamber in the sublimation purification apparatus of FIG. 3.
  • 7 is a perspective view showing a state in which the tube housing and the boat are in close contact in FIG. 4.
  • the tube housing 200 has a movement path of a sublimation purification target material to be captured in the second boat 300b after the sublimation purification target material contained in the first boat 300a is heated.
  • a sublimation purification target material to be captured in the second boat 300b after the sublimation purification target material contained in the first boat 300a is heated.
  • Substances subject to sublimation purification may be mixed materials in which organic substances and impurities are mixed.
  • the heating part 400 positioned adjacent to the outer surface of the tube housing 200 includes a first heating zone 410 and a first boat 300a located in a portion corresponding to the first boat 300a. And a second heating zone 420 positioned between the second boat 300b and a third heating zone 430 positioned at a portion corresponding to the second boat 300b.
  • Sublimation purification target material contained in the first boat 300a is heated and liquefied by the lower heating unit 440 located under the first boat 300a, and the temperature of the sublimation purification target is further increased by gas.
  • the gas-activated sublimation material reaches the first first heating zone 410 of the tube housing 200 and then moves to the second heating zone 420 having a low temperature.
  • the first heating zone 410 maintains a gas state by maintaining a temperature condition equivalent to that of the first boat 300a, and allows the sublimation material in the gas state to fly to the second heating zone 420.
  • the second heating zone 420 may lower the temperature to phase change the sublimation purification target material activated with the gas into a liquid state.
  • the second heating zone 420 may also have a cooling function in order to control phase changes between materials due to excessive heat interference of the first heating zone 410.
  • the material liquefied in the second heating zone 420 enters the third heating zone 430, and the third heating zone 430 controls the temperature to maintain the temperature of the solution state of the sublimated purification target material. Make it possible. Substances subject to sublimation purification through the third heating zone 430 are dropped into a solution state in the second boat 300b.
  • the tube housing 200 may have a tilted structure along a movement path of a sublimation purification target material. Due to the tilted structure, the material can be smoothly moved from the first boat 300a to the second boat 300b.
  • the structure of the tilt is to allow the material to be purified to be sublimated to flow well to the second boat 300b.
  • the tilted degree may be approximately 5 degrees.
  • the boat 300 loaded through the gate 700 in FIG. 3 and loaded inside the chamber 120 may be in close contact with the tube housing 200 by the vertical transfer device 800.
  • the vertical transfer device 800 moves the boat 300 in the chamber 120 so that the loaded boat 300 is in close contact with the tube housing 200 located in the chamber 120 so that a sublimation purification process can be performed. Can play a role.
  • the vertical transfer device 800 may be a pneumatic sealer.
  • the transfer robot 650 described in FIG. 3 moves the first boat 300a while the lower heating units 440 and 450 mounted below the first boat 300a are lowered by the vertical transfer device 800. It can be mounted on the second chamber 120. Subsequently, by closing the gate and creating a vacuum atmosphere, the lower heating units 440 and 450 are raised toward the tube housing 200 by using the up-and-down transfer device 800, so that the first mounted in the second chamber 120 is mounted.
  • the boat 300a may be tightly coupled to the tube housing 200 by physical force. Since the first boat 300a and the tube housing 200 are in close contact / combination, it is possible to prevent external contamination that may occur due to the gasified material being lost into the gap between the first boat 300a and the tube housing 200.
  • the second boat 300b exists in a separate state from the tube housing 200, so that the sublimation is performed while the first boat 300a and the tube housing 200 are kept in close contact with each other.
  • the second boat 300b collects the liquefied material.
  • the material liquefied by the inclined angle according to the tilt structure of the tube housing 200 may be collected in the second boat 300b through the phenomenon of falling from top to bottom.
  • the internal pressure of the second chamber 120 and the internal pressure of the tube housing 200 may be maintained the same.
  • the sealing gasket 250 is interposed between the bow 300 and the tube housing 200. It may further include.
  • the sealing gasket 250 is formed at the end of the tube housing 200, and the sealing gasket 250 fills a narrow gap occurring in a portion where the end of the tube housing 200 is bent.
  • the sealing gasket 250 may include at least one of titanium (Ti), silver (Ag), copper (Cu), and ceramic.
  • the sealing gasket 250 becomes a fluid when the solid is heated in the chamber 120, and this fluid can be prevented from leaking out of the tube housing.
  • FIG. 8 is a perspective view showing a heating unit according to an embodiment of the present invention.
  • the tube housing 200 may have a tub shape, and the tub may have an inverted structure.
  • the first boat 300a and the second boat 300b are in close contact with both edges of the tube housing 200, respectively.
  • the heating unit includes an upper heating unit positioned adjacent to the outer surface of the tube housing 200 and a lower heating unit positioned adjacent to the outer surfaces of the first and second boats 300a and 300b.
  • the upper heating part includes a first heating zone 410 positioned in a portion corresponding to the first boat 300a, a second heating zone 420 positioned between the first boat 300a and the second boat 300b, and It includes a third heating zone 430 located in the portion corresponding to the second boat (300b).
  • the lower heating part includes a fourth heating zone 440 surrounding the side surface of the first boat 300a and a fifth heating zone 450 surrounding the side surface of the second boat 300b.
  • the heating unit according to the present embodiment may be formed of tantalum. Since tantalum is excellent in ductility, easy to process, and has good thermal conductivity and electrical conductivity, independent heat transfer is possible in the heating zone to be heated, and heat transfer control can be very stable.
  • the heating portion may be formed of Inconel. Inconel has good heat resistance and does not oxidize even in an oxidizing condition of about 900 degrees Celsius or higher, and may have excellent properties such as elongation, tensile strength, and yield point that do not change up to 600 degrees Celsius.
  • FIG. 9 is a view showing a state in which the boat is in close contact with the tube housing in one chamber of the sublimation purification apparatus according to another embodiment of the present invention.
  • 10 is a perspective view showing a vertical transfer device and a sublimation purification amount measuring member in part A of FIG. 9.
  • 11 is a front view showing the sublimation purification amount measuring member of FIG. 10.
  • the sublimation purification apparatus further includes a sublimation purification amount measuring member 850 fixed inside the chamber 120.
  • the sublimation purification amount measuring member 850 may be located under the boat 300. As such, the sublimation purification amount measurement member 850 is located at the bottom of the boat 300, so that the sublimation purification amount can be checked in real time during the sublimation purification process.
  • the sublimation purification amount measuring member 850 is a transducer for measuring force or load as a load sensor, and is a device capable of outputting an output as an electrical signal.
  • the heating part 440 which is a heating part located at the bottom of the bow 300, surrounds the bow 300, but the sublimation purification amount measuring member 850 according to this embodiment has a heating part 440.
  • a tripod-shaped pin 860 protrudes from a portion that does not interfere with the heating portion 440.
  • the heating unit 440 may be a wire-type heating wire, and the heating wire is formed in a plurality while having a gap, thereby enclosing the tube housing 200 as shown in FIG. 9. In other words, between the plurality of heating wires, the tripod-shaped pin 860 protrudes upward, so that the boat 300 and the sublimation purification amount measuring member 850 can be assembled without interference from the heating unit 440.
  • the boat 300 moves downward by the vertical transfer device 800 supporting the boat 300, the boat 300 reaches the pin 860 of the sublimation purification amount measuring member 850. At this time, the purification amount of the sublimation purification material in the boat 300 can be measured.
  • the sublimation purification device uses a sublimation purification amount measurement member 850 Therefore, it is possible to check the material movement amount and material consumption in real time during the process, thereby minimizing the deviation between processes and problems that may occur in the process.
  • the first chamber 300 loaded with the sublimation purification target material in the first chamber 110 is loaded and heated to be mixed with the sublimation purification target material Outgassing and other impurities are removed first.
  • the purified material residual solvent and monomolecular impurities are first sublimed and trapped in the second boat 300b. Thereafter, the temperature is not sublimated, that is, cooled to a temperature in a range that is not gasified.
  • the first boat 300a containing the first purified material in the first chamber 110 is unloaded from the first chamber 110, and the first boat is transferred to the second chamber 120 through the transfer robot 650 ( 300a).
  • the sublimation purification target material contained in the first boat 300a loaded in the second chamber 120 is heated to a fourth heating zone 440 to be solutiond, and the temperature is further increased to activate the gas.
  • the sublimation material activated by gas moves to the first heating zone 410, and the sublimation material activated by gas maintains the same temperature as the first boat 300a in the first heating zone 410 so that the sublimation material activated by gas is the second heating zone ( 420).
  • the sublimation purification target material activated with the gas is solutiond.
  • the substance liquefied in the second heating zone 420 enters the third heating zone 430, and controls the third heating zone 430 to maintain the temperature of the solution state of the solution-sublimed purification target material. 2 Drop to the boat (300b) in a solution state and capture. After the process is completed in the second chamber 120, the second boat 300b is moved to the cooling chamber 150 using the transfer robot 650, and the second boat 300b loaded in the cooling chamber 150 The solution material contained in can be cooled.
  • a process sequentially performed in the first chamber 110 and the second chamber 120 is performed. , It may be repeatedly performed in the third chamber 130 and the fourth chamber 140.
  • the first boat 300a, the second boat 300b, and the tube housing 200 are formed of metal, and the sublimation purification method according to the present embodiment may further include cleaning a chemical solution of parts formed of the metal. have. Through such a cleaning process, metal impurities eluted from the metal component material constituting the heating part, the boat, and the tube housing during high vacuum are mixed in the sublimation purification target material, thereby preventing problems such as an increase in voltage and a shortened lifespan when filing an organic light emitting device. have.
  • the sublimation purification method according to the present embodiment may further include baking after the washing step. Baking may be performed at a temperature of about 200 degrees Celsius or higher, and may be performed at least twice.
  • heating zone 410, 420, 430, 440, 450: heating zone

Abstract

A sublimation purification apparatus, according to one embodiment of the present invention, comprises: a vacuum chamber; a tube housing disposed within the vacuum chamber; a boat in close contact with the tube housing; and a heating unit positioned adjacent to an outer surface of the boat and an outer surface of the tube housing, wherein the boat contains a material subject to sublimation purification, and at least one of the boat and the tube housing is formed of a metal.

Description

승화 정제 장치 및 승화 정제 방법Sublimation purification device and sublimation purification method
관련 출원(들)과의 상호 인용Cross-citation with relevant application (s)
본 출원은 2018년 9월 12일자 한국 특허 출원 제10-2018-0109089호 및 2019년 6월 4일자 한국 특허 출원 제10-2019-0066109에 기초한 우선권의 이익을 주장하며, 해당 한국 특허 출원의 문헌에 개시된 모든 내용은 본 명세서의 일부로서 포함된다.This application claims the benefit of priority based on Korean Patent Application No. 10-2018-0109089 dated September 12, 2018 and Korean Patent Application No. 10-2019-0066109 dated June 4, 2019, and documents of the Korean patent application All content disclosed in is included as part of this specification.
본 발명은 승화 정제 장치 및 승화 정제 방법에 관한 것으로서, 보다 구체적으로 고순도의 정제 효율을 갖고 연속 공정으로 인한 수율 향상 및 생산 시간 단축을 구현할 수 있는 승화 정제 장치 및 승화 정제 방법에 관한 것이다.The present invention relates to a sublimation purification apparatus and a sublimation purification method, and more particularly, to a sublimation purification apparatus and a sublimation purification method capable of realizing a high-purity purification efficiency and improving yield due to a continuous process and reducing production time.
전계 발광 소자는 전자와 정공의 재결합으로 형광체를 발광시키는 자발광 소자로서, 전계 발광 소자의 발광 특성에 영향을 미치는 요인으로는 발광층 물질의 순도가 있을 수 있고, 특히, 유기 전계 발광 소자의 경우 유기 물질의 순도는 소자의 발광 특성에 매우 큰 영향을 미치게 된다. 유기 물질 중에 불순물이 혼합되어 있으면, 그 불순물이 캐리어의 트랩이 되거나 소광의 원인이 되어 소자의 발광 강도 및 발광 효율이 크게 저하되는 원인이 되기 때문에 이러한 불순물을 제거하기 위해 유기 물질을 정제할 필요가 있다.The electroluminescent device is a self-luminous device that emits phosphors by recombination of electrons and holes, and may have a purity of a light-emitting layer material as a factor affecting the luminescence properties of the electroluminescent device. In particular, in the case of an organic electroluminescent device, organic The purity of the material greatly affects the luminescence properties of the device. When impurities are mixed in the organic material, it is necessary to purify the organic material in order to remove these impurities because the impurities become a trap of carriers or cause quenching, which significantly decreases the luminous intensity and luminous efficiency of the device. have.
이러한 유기 물질의 정제 방법으로는 일반적으로 용매를 사용한 재결정 또는 승화에 의한 재결정 방법이 사용된다. 승화에 의한 재결정 방법이 진공 하에서 유기 물질이 승화되어 재결정되므로 불순물이 들어가지 않는 특성을 갖게 되어 통상적으로 유기 전계 발광 소자용 유기 물질의 정제에는 연속 승화 정제법(train-sublimation)을 사용할 수 있다. 이러한 방법은 도 1에 도시된 원리도에서 볼 수 있듯이, 제1 히팅존(1)에서 정제 물질과 불순물이 포함된 유기 물질(6)을 가열하여 기화시키면, 기체들은 석영 튜브(5)를 통하여 펌핑되는 방향으로 분자 이동을 하게 되고, 이때 다른 온도 영역을 갖는 제2 히팅존(2)과 제3 히팅존(3)을 만나면서 상변화하여 액화 또는 고화되면서 정제 물질(7)과 불순물(8)을 분리 수집할 수 있는 것이다.As a method for purifying the organic material, a recrystallization method using a solvent or recrystallization using a solvent is generally used. Since the recrystallization method by sublimation has an organic substance sublimation and recrystallization under vacuum, it has a property that impurities do not enter, and thus, a conventional train-sublimation method may be used for purification of an organic material for an organic EL device. This method, as can be seen in the principle diagram shown in Figure 1, the first heating zone (1) by heating and vaporizing the organic material (6) containing the purified material and impurities, the gases through the quartz tube (5) Molecular movement is performed in the direction of pumping, and at this time, the phase changes while liquefying or solidifying while meeting the second heating zone 2 and the third heating zone 3 having different temperature regions, thereby purifying the purified material 7 and impurities 8 It can be collected separately.
종래의 승화 정제 장치는 도 2에 도시된 바와 같이, 진공을 위한 제1 석영관(10)의 내부에 수 개의 제2 석영관(20)을 설치하되, 제1 석영관(10)의 외측에는 세라믹 히터(31)가 구비된 히터 커버(30)를 설치하여 이루어질 수 있다. 이와 같은 승화 정제 장치로 유기 물질(51)을 투입한 후 히터 커버(30)를 닫고 세라믹 히터(31)를 가열하게 되면, 승화 장치 내부의 온도 기울기로 인해 정제 물질(52)과 불순물(53)의 분리가 이루어지게 된다.As shown in FIG. 2, the conventional sublimation purification apparatus is provided with several second quartz tubes 20 inside the first quartz tube 10 for vacuum, but outside the first quartz tube 10 It can be made by installing a heater cover 30 is provided with a ceramic heater (31). When the organic material 51 is introduced into the sublimation purification device, and the heater cover 30 is closed and the ceramic heater 31 is heated, the purification material 52 and impurities 53 due to the temperature gradient inside the sublimation device Separation is achieved.
이러한 승화 정제 장치에서 제1 석영관(10)은 진공 분위기나 대기와의 기밀을 위해 사용되고, 제2 석영관(20)은 다수의 구간으로 분리하여 서로 다른 온도로 제어함으로써 유기 물질(51)의 불순물을 제거하여 정제 물질(52)을 얻어내게 된다. 하지만, 승화 정제 장치의 내부 재질은 석영(Quartz)은 그 재료가 가지는 단점 때문에 대용량으로 양산하지 못하는 한계 및 공정 연속성을 갖기 어려운 문제 때문에 수율이 저하되고 인력이 증가하는 단점이 있다.In this sublimation purification device, the first quartz tube 10 is used for airtightness with a vacuum atmosphere or the atmosphere, and the second quartz tube 20 is separated into a plurality of sections and controlled at different temperatures to control the organic material 51. Purification material 52 is obtained by removing impurities. However, the internal material of the sublimation purification device has the disadvantage that the yield is lowered and the manpower is increased due to the limitations of mass production due to the disadvantages of the material and the difficulty of having the process continuity.
본 발명이 해결하고자 하는 과제는, 정제기 내부 재질인 석영의 설계 가공의 한계 및 내구성이 약한 단점을 보완하기 위해 내부 물질의 금속화를 통해 공정 연속 자동화, 고순도 정제 효율, 연속 공정으로 인한 수율 향상 및 생산 시간 단축 등을 구현하는 승화 정제 장치 및 승화 정제 방법을 제공하기 위한 것이다.The problem to be solved by the present invention is to improve the process continuous automation through metallization of the internal material, high purity purification efficiency, yield improvement due to the continuous process, and metallization of the internal material to compensate for the limitations of the design process limitation and the durability of the quartz, which is the material of the refiner, and It is to provide a sublimation purification apparatus and a sublimation purification method that realizes a reduction in production time and the like.
그러나, 본 발명의 실시예들이 해결하고자 하는 과제는 상술한 과제에 한정되지 않고 본 발명에 포함된 기술적 사상의 범위에서 다양하게 확장될 수 있다.However, the problems to be solved by the embodiments of the present invention are not limited to the above-described problems and can be variously extended within the scope of the technical spirit included in the present invention.
본 발명의 일 실시예에 따른 승화 정제 장치는 진공 챔버, 상기 진공 챔버 내에 위치하는 튜브 하우징, 상기 튜브 하우징에 밀착되어 있는 보우트 그리고 상기 보우트의 바깥면 및 상기 튜브 하우징 바깥면에 인접하여 위치하는 히팅부를 포함하고, 상기 보우트에 승화 정제 대상 물질이 담기고, 상기 보우트 및 상기 튜브 하우징 중 적어도 하나는 금속으로 형성된다.An apparatus for sublimation purification according to an embodiment of the present invention includes a vacuum chamber, a tube housing positioned in the vacuum chamber, a boat in close contact with the tube housing, and a heating positioned adjacent to the outer surface of the tube and the outer surface of the tube housing It includes a portion, and the sublimation target material is contained in the boat, and at least one of the boat and the tube housing is formed of metal.
상기 보우트는 제1 보우트 및 제2 보우트를 포함하고, 상기 제1 보우트와 상기 제2 보우트는 상기 진공 챔버 내에 함께 위치하고, 상기 튜브 하우징이 이동 경로가 되어 상기 제1 보우트에 담긴 승화 정제 대상 물질이 가열된 이후 상기 제2 보우트에 포획되도록 할 수 있다.The boat includes a first boat and a second boat, and the first boat and the second boat are located together in the vacuum chamber, and the tube housing becomes a movement path, whereby the sublimation purification material contained in the first boat is After being heated, it can be allowed to be captured in the second boat.
상기 튜브 하우징 바깥면에 인접하여 위치하는 히팅부는 상기 제1 보우트에 대응하는 부분에 위치하는 제1 히팅존, 상기 제1 보우트와 상기 제2 보우트 사이에 위치하는 제2 히팅존 및 상기 제2 보우트에 대응하는 부분에 위치하는 제3 히팅존을 포함하고, 상기 제1 히팅존은 상기 제1 보우트에 담겨 기체로 활성화된 승화 정제 대상 물질이 기체 상태를 유지하도록 온도를 컨트롤하고, 상기 제2 히팅존은 상기 기체로 활성화된 승화 정제 대상 물질을 용액화하며, 상기 제3 히팅존은 상기 용액화된 승화 정제 대상 물질의 용액 상태를 유지하도록 온도를 컨트롤하여 상기 제2 보우트에 용액 상태의 승화 정제 대상 물질이 떨어지도록 할 수 있다.The heating unit located adjacent to the outer surface of the tube housing is a first heating zone located in a portion corresponding to the first boat, a second heating zone located between the first boat and the second boat, and the second boat It includes a third heating zone located in the portion corresponding to, the first heating zone is the sublimation purification target material activated by the gas contained in the first boat to control the temperature to maintain the gas state, the second heating The zone is to sublimate the substance to be purified sublimation activated by the gas, and the third heating zone is to control the temperature to maintain the solution status of the substance to be sublimated purification to sublimate purification in the solution state to the second boat. You can make the target material fall.
상기 튜브 하우징은 상기 승화 정제 대상 물질의 이동 경로를 따라 틸트된 구조를 가질 수 있다.The tube housing may have a tilted structure along the movement path of the sublimation purification target material.
상기 금속은 티타늄 또는 탄탈륨을 포함할 수 있다.The metal may include titanium or tantalum.
상기 승화 정제 장치는 상기 튜브 하우징의 단부에 형성된 실링 가스켓을 더 포함하고, 상기 튜브 하우징과 상기 보우트 사이에 상기 실링 가스켓이 개재될 수 있다.The sublimation purification device further includes a sealing gasket formed at an end of the tube housing, and the sealing gasket may be interposed between the tube housing and the boat.
상기 실링 가스켓은 티타늄(Ti), 은(Ag), 구리(Cu) 및 세라믹 중 적어도 하나를 포함할 수 있다.The sealing gasket may include at least one of titanium (Ti), silver (Ag), copper (Cu), and ceramic.
본 발명의 다른 일 실시예에 따른 승화 정제 장치는 챔버 이동부, 상기 챔버 이동부에 인접하여 위치하는 복수의 챔버, 상기 챔버 내에 위치하는 튜브 하우징, 상기 챔버 이동부와 상기 챔버들 사이에 위치하는 게이트, 이송 로봇에 의해 상기 챔버 이동부 내부를 이동하거나 상기 챔버 이동부에서 상기 챔버 내부로 로딩 또는 언로딩되는 보우트 그리고 상기 보우트의 바깥면 및 상기 튜브 하우징 바깥면을 둘러싸는 히팅부를 포함하고, 상기 보우트는 상기 튜브 하우징으로 서로 연결되는 제1 보우트와 제2 보우트를 포함한다.The sublimation purification apparatus according to another embodiment of the present invention includes a chamber moving part, a plurality of chambers located adjacent to the chamber moving part, a tube housing located in the chamber, and located between the chamber moving part and the chambers A gate, a boat moving inside the chamber moving part by a transfer robot or loading or unloading from the chamber moving part into the chamber, and a heating part surrounding the outer surface of the boat and the outer surface of the tube housing, The boat includes a first boat and a second boat connected to each other with the tube housing.
상기 튜브 하우징 바깥면에 인접하여 위치하는 히팅부는 상기 제1 보우트에 대응하는 부분에 위치하는 제1 히팅존, 상기 제1 보우트와 상기 제2 보우트 사이에 위치하는 제2 히팅존 및 상기 제2 보우트에 대응하는 부분에 위치하는 제3 히팅존을 포함하고, 상기 제1 히팅존은 상기 제1 보우트에 담겨 기체로 활성화된 승화 정제 대상 물질이 기체 상태를 유지하도록 온도를 컨트롤하고, 상기 제2 히팅존은 상기 기체로 활성화된 승화 정제 대상 물질을 용액화하며, 상기 제3 히팅존은 상기 용액화된 승화 정제 대상 물질의 용액 상태를 유지하도록 온도를 컨트롤하여 상기 제2 보우트에 용액 상태의 승화 정제 대상 물질이 떨어지도록 할 수 있다.The heating unit located adjacent to the outer surface of the tube housing is a first heating zone located in a portion corresponding to the first boat, a second heating zone located between the first boat and the second boat, and the second boat It includes a third heating zone located in the portion corresponding to, the first heating zone is the sublimation purification target material activated by the gas contained in the first boat to control the temperature to maintain the gas state, the second heating The zone is to sublimate the substance to be purified sublimation activated by the gas, and the third heating zone is to control the temperature to maintain the solution status of the substance to be sublimated purification to sublimate purification in the solution state to the second boat. You can make the target material fall.
상기 튜브 하우징은 상기 승화 정제 대상 물질의 이동 경로를 따라 틸트된 구조를 가질 수 있다.The tube housing may have a tilted structure along the movement path of the sublimation purification target material.
상기 승화 정제 장치는 상기 제1 보우트와 상기 제2 보우트 중 적어도 하나는 상기 게이트를 통과한 보우트를 상기 챔버 내에서 이동시켜 상기 튜브 하우징과 밀착되도록 하는 상하 이송 장치를 더 포함할 수 있다.The sublimation purification device may further include an up-and-down transfer device that moves at least one of the first and second boats to the tube housing by moving the boat passing through the gate in the chamber.
상기 보우트 및 상기 튜브 하우징 중 적어도 하나는 금속으로 형성될 수 있다.At least one of the boat and the tube housing may be formed of metal.
상기 승화 정제 장치는 상기 튜브 하우징의 단부에 형성된 실링 가스켓을 더 포함하고, 상기 보우트가 상기 챔버 내부로 로딩되어 상기 튜브 하우징과 맞물릴 때, 상기 보우트와 상기 튜브 하우징 사이에 상기 실링 가스켓이 개재될 수 있다.The sublimation purification apparatus further includes a sealing gasket formed at an end of the tube housing, and when the boat is loaded into the chamber and engaged with the tube housing, the sealing gasket is interposed between the tube and the tube housing. You can.
상기 복수의 챔버는 서로 이웃하는 제1 챔버와 제2 챔버를 포함하고, 상기 제1 챔버에 위치하는 튜브 하우징은 상기 제1 챔버에 로딩된 제1 보우트에 담긴 승화 정제 대상 물질을 가열하여 제거된 불순물이 상기 제2 보우트에 포획되고, 상기 제1 챔버로부터 언로딩된 제1 보우트가 상기 챔버 이동부를 통해 상기 제2 챔버에 로딩되며, 상기 제2 챔버에 로딩된 제1 보우트에 담긴 승화 정제 대상 물질이 용융화하여 기체로 활성화될 수 있다.The plurality of chambers includes a first chamber and a second chamber adjacent to each other, and the tube housing positioned in the first chamber is removed by heating a sublimation purification target material contained in the first boat loaded in the first chamber Sublimation purification targets contained in the first boat loaded into the second chamber, where impurities are captured in the second boat, the first boat unloaded from the first chamber is loaded into the second chamber through the chamber moving part, and The material can be melted and activated with gas.
상기 승화 정제 장치는 상기 챔버 내부에 고정되어 있는 승화 정제량 측정 부재를 더 포함하고, 상기 승화 정제량 측정 부재는 상기 보우트의 하부에 위치할 수 있다.The sublimation purification device may further include a sublimation purification amount measurement member fixed inside the chamber, and the sublimation purification amount measurement member may be located below the boat.
상기 승화 정제 장치는 상기 제1 보우트와 상기 제2 보우트 중 적어도 하나는 상기 게이트를 통과한 보우트를 상기 챔버 내에서 이동시켜 상기 튜브 하우징과 밀착되도록 하는 상하 이송 장치를 더 포함할 수 있다.The sublimation purification device may further include an up-and-down transfer device that moves at least one of the first and second boats to the tube housing by moving the boat passing through the gate in the chamber.
상기 이송 장치에 의해 상기 보우트가 상기 튜브 하우징으로부터 이격되어 상기 승화 정제량 측정 부재에 도달하여 승화 정제량을 측정할 수 있다.The boat may be spaced apart from the tube housing by the transfer device to reach the sublimation purification amount measurement member to measure the sublimation purification amount.
본 발명의 다른 일 실시예에 따른 승화 정제 방법은 제1 챔버 내에 승화 정제 대상 물질이 담긴 제1 보우트를 로딩하는 단계, 상기 로딩된 제1 보우트에 담긴 상기 승화 정제 대상 물질을 가열하여 제거된 불순물을 튜브 하우징을 통해 제2 보우트에 포획하는 단계, 상기 제1 챔버로부터 상기 제1 보우트를 언로딩하여 이송 로봇을 통해 제2 챔버에 상기 제1 보우트를 로딩하는 단계, 상기 제2 챔버에 로딩된 제1 보우트에 담긴 상기 승화 정제 대상 물질을 용융화하여 기체로 활성화시키는 단계, 상기 기체로 활성화된 물질을 용액화하는 단계, 상기 용액화된 물질을 상기 제2 챔버에 포함된 튜브 하우징을 통해 상기 제2 챔버 내에 위치하는 제2 보우트에 포획하는 단계, 상기 제2 챔버 내에 위치하는 상기 제2 보우트를 상기 이송 로봇을 사용하여 냉각 챔버로 이동하는 단계 그리고 상기 냉각 챔버에 로딩된 상기 제2 보우트에 담긴 상기 용액화된 물질을 냉각하는 단계를 포함하고, 상기 제1 보우트, 상기 제2 보우트 및 상기 튜브 하우징 중 적어도 하나는 금속으로 형성된다.The sublimation purification method according to another embodiment of the present invention comprises loading a first boat containing a sublimation purification target material in a first chamber, and impurities removed by heating the sublimation purification target material contained in the loaded first boat Capturing to the second boat through the tube housing, unloading the first boat from the first chamber and loading the first boat into the second chamber through a transfer robot, loaded into the second chamber Melting the sublimation purification target material contained in the first boat and activating it with gas, liquefying the gas-activated material, and transporting the solution through the tube housing included in the second chamber; Capturing to a second boat located in the second chamber, the second boat located in the second chamber to the cooling chamber using the transfer robot And cooling the liquefied material contained in the second boat loaded in the cooling chamber, wherein at least one of the first boat, the second boat and the tube housing is formed of metal. .
상기 승화 정제 방법은 상기 제1 보우트, 상기 제2 보우트 및 상기 튜브 하우징 중 금속으로 형성된 부품을 화학 용액 세정하는 단계를 더 포함할 수 있다.The sublimation purification method may further include cleaning a chemical solution of parts formed of a metal in the first boat, the second boat, and the tube housing.
상기 승화 정제 방법은 상기 세정하는 단계 이후에 베이킹하는 단계를 더 포함할 수 있다.The sublimation purification method may further include baking after the washing step.
본 발명의 다른 일 실시예에 따른 유기 발광 소자용 물질은, 앞에서 설명한 승화 정제 방법에 의해 정제된다.The material for an organic light emitting device according to another embodiment of the present invention is purified by the sublimation purification method described above.
본 발명의 다른 일 실시예에 따른 유기 발광 소자는, 앞에서 설명한 유기 발광 소자용 물질을 포함한다.The organic light emitting device according to another embodiment of the present invention includes a material for an organic light emitting device described above.
실시예들에 따르면, 기존의 정제기 내부 재질로 석영을 사용하는 것을 금속으로 대체하여, 석영 재질의 단점으로 인해 어려운 대용량으로 정제 물질 생산, 공정 연속성에 따라 수율 향상시킬 수 있다.According to embodiments, it is possible to improve the yield according to the continuity of the production and purification of the purified material with a large capacity, which is difficult due to the disadvantages of the quartz material, by replacing the existing quartz refiner with a metal.
또, 복수의 챔버에서 불순물 정제가 이루어지고, 게이트 및 로봇에 의해 보우트가 이동함으로써 각 정제 단계에서의 경계가 명확하므로 고순도 정제 효율을 높일 수 있다.In addition, since impurities are purified in a plurality of chambers and the boat is moved by a gate and a robot, the boundary in each purification step is clear, so that high-purity purification efficiency can be improved.
또, 고진공으로 이루어지는 정제 작업에서 내부 재질인 석영의 파손 및 내구성의 강도 저하로 발생할 수 있는 안정 사고 위험성을 줄일 수 있다.In addition, it is possible to reduce the risk of stable accidents that may occur due to the damage of the internal material quartz and the strength of durability in the purification operation made of high vacuum.
도 1은 유기 물질의 정제 원리도를 나타낸다.1 shows a principle diagram of purification of an organic material.
도 2는 종래의 정제 장치를 나타내는 단면도이다.2 is a cross-sectional view showing a conventional purification device.
도 3은 본 발명의 일 실시예에 따른 승화 정제 장치를 나타내는 개략적인 도면이다.Figure 3 is a schematic diagram showing a sublimation purification apparatus according to an embodiment of the present invention.
도 4는 도 3의 승화 정제 장치에서 하나의 챔버 내 위치하는 튜브 하우징과 보우트가 밀착된 형태를 확대하여 나타내는 도면이다.FIG. 4 is an enlarged view showing a form in which the tube housing and the boat located in one chamber are closely attached in the sublimation purification apparatus of FIG. 3.
도 5는 도 4의 승화 정제 장치에서 튜브 하우징 일부가 틸트된 구조를 갖는 변형 실시예를 나타내는 도면이다.FIG. 5 is a view showing a modified embodiment in which a part of the tube housing has a tilted structure in the sublimation purification device of FIG. 4.
도 6은 도 3의 승화 정제 장치에서 챔버 내부로 보우트가 로딩되는 모습을 나타내는 도면이다.FIG. 6 is a view showing a state in which the boat is loaded into the chamber in the sublimation purification apparatus of FIG. 3.
도 7은 도 4에서 튜브 하우징과 보우트가 밀착된 모습을 나타내는 사시도이다.7 is a perspective view showing a state in which the tube housing and the boat are in close contact in FIG. 4.
도 8은 본 발명의 일 실시예에 따른 히팅부를 나타내는 사시도이다.8 is a perspective view showing a heating unit according to an embodiment of the present invention.
도 9는 본 발명의 다른 일 실시예에 따른 승화 정제 장치의 한 챔버 내에서 보우트가 튜브 하우징에 밀착된 상태를 나타내는 도면이다.9 is a view showing a state in which the boat is in close contact with the tube housing in one chamber of the sublimation purification apparatus according to another embodiment of the present invention.
도 10은 도 9의 A부분에서 상하 이송 장치와 승화 정제량 측정 부재를 나타내는 사시도이다.10 is a perspective view showing a vertical transfer device and a sublimation purification amount measuring member in part A of FIG. 9.
도 11은 도 10의 승화 정제량 측정 부재를 나타내는 정면도이다.11 is a front view showing the sublimation purification amount measuring member of FIG. 10.
이하, 첨부한 도면을 참고로 하여 본 발명의 여러 실시예들에 대하여 본 발명이 속하는 기술 분야에서 통상의 지식을 가진 자가 용이하게 실시할 수 있도록 상세히 설명한다. 본 발명은 여러 가지 상이한 형태로 구현될 수 있으며 여기에서 설명하는 실시예들에 한정되지 않는다.Hereinafter, various embodiments of the present invention will be described in detail with reference to the accompanying drawings so that those skilled in the art to which the present invention pertains can easily practice. The present invention can be implemented in many different forms and is not limited to the embodiments described herein.
또한, 명세서 전체에서, 어떤 부분이 어떤 구성요소를 "포함" 한다고 할 때, 이는 특별히 반대되는 기재가 없는 한 다른 구성요소를 제외하는 것이 아니라 다른 구성요소를 더 포함할 수 있는 것을 의미한다.Also, in the specification, when a part “includes” a certain component, it means that the component may further include other components, not to exclude other components, unless otherwise stated.
또한, 명세서 전체에서, "평면상"이라 할 때, 이는 대상 부분을 위에서 보았을 때를 의미하며, "단면상"이라 할 때, 이는 대상 부분을 수직으로 자른 단면을 옆에서 보았을 때를 의미한다.In addition, throughout the specification, when referred to as "planar", this means when the object portion is viewed from above, and when it is referred to as "cross-sectional", it means when the cross section of the object portion vertically cut is viewed from the side.
도 3은 본 발명의 일 실시예에 따른 승화 정제 장치를 나타내는 개략적인 도면이다.Figure 3 is a schematic diagram showing a sublimation purification apparatus according to an embodiment of the present invention.
도 3을 참고하면, 본 실시예에 따른 승화 정제 장치(1000)는 챔버 이동부(600), 복수의 챔버(110, 120, 130, 140) 및 챔버 이동부(600)와 챔버(110, 120, 130, 140) 사이에 위치하는 게이트(700)를 포함한다. 각 챔버(110, 120, 130, 140) 내에는 튜브 하우징(200)이 위치하고, 튜브 하우징(200)에 의해 2개의 보우트(300)가 서로 연결될 수 있다. 보우트(300)는 튜브 하우징(200)에 밀착되어 승화 정제 공정이 진행될 수 있다. 복수의 챔버(110, 120, 130, 140) 각각은 진공 챔버일 수 있다. 챔버 이동부(600)도 진공 상태를 유지하는 것이 바람직하다.Referring to FIG. 3, the sublimation purification apparatus 1000 according to the present embodiment includes a chamber moving part 600, a plurality of chambers 110, 120, 130, 140, and a chamber moving part 600 and chambers 110, 120 , 130, 140. The tube housing 200 is located in each chamber 110, 120, 130, 140, and two boats 300 can be connected to each other by the tube housing 200. The bow 300 may be in close contact with the tube housing 200 to perform a sublimation purification process. Each of the plurality of chambers 110, 120, 130, and 140 may be a vacuum chamber. It is preferable that the chamber moving part 600 also maintains a vacuum state.
승화 정제 장치(1000)는, 챔버(110, 120, 130, 140) 내부에 위치하는 튜브 하우징(200)의 바깥면에 인접하여 위치하는 히팅부(400) 및 히팅부(400)를 덮는 냉각부(500)를 포함한다. 보우트(300) 바깥면에 인접한 부분에도 히팅부(400)가 형성되어 있다.The sublimation purification apparatus 1000 includes a heating unit 400 and a cooling unit covering the heating unit 400 located adjacent to the outer surface of the tube housing 200 located inside the chambers 110, 120, 130, and 140. 500. The heating part 400 is also formed in a portion adjacent to the outer surface of the boat 300.
본 실시예에 따른 승화 정제 장치(1000)는, 승화 정제 공정의 마지막 단계에서 유기 발광 소자용 물질을 회수하기 위해, 복수의 챔버(110, 120, 130, 140) 외에 냉각 챔버(150)를 더 포함할 수 있다. 냉각 챔버(150) 내부에는 다른 챔버(110, 120, 130, 140) 내부에 위치하는 튜브 하우징(200)이 없고, 냉각부(500)만 포함될 수 있다. 냉각 챔버(150)는 정제 공정을 마친 후에 이송 로봇(650)에 의해 정제된 물질이 담긴 보우트(300)가 게이트(700)를 통과하여 냉각 챔버(150)에 로딩되면, 용액 상태의 정제 물질이 냉각되어 제품으로 사용하기 위한 유기 발광 소자용 물질을 회수할 수 있다.The sublimation purification apparatus 1000 according to the present embodiment further includes a cooling chamber 150 in addition to the plurality of chambers 110, 120, 130 and 140 in order to recover the material for the organic light emitting device in the final step of the sublimation purification process It can contain. Inside the cooling chamber 150, there is no tube housing 200 located inside the other chambers 110, 120, 130, 140, and only the cooling unit 500 may be included. Cooling chamber 150, after the purification process, when the boat 300 containing the material purified by the transfer robot 650 passes through the gate 700 and is loaded into the cooling chamber 150, the purified material in solution state After cooling, the material for an organic light emitting device for use as a product can be recovered.
챔버 이동부(600)에는 이송 로봇(650)이 위치하고, 보우트(300)가 이송 로봇(650)에 의해 챔버 이동부(600) 내부를 이동하거나 챔버 이동부(600)에서 각 챔버(110, 120, 130, 140, 150)로 로딩되거나 언로딩될 수 있다. 챔버 이동부(600)에서 각 챔버(110, 120, 130, 140, 150)로 보우트(300)가 로딩 또는 언로딩될 때, 챔버 이동부(600)와 각 챔버(110, 120, 130, 140, 150) 사이에 위치하는 게이트(700)를 보우트(300)가 통과할 수 있다. 게이트(700)를 통과하여 챔버(110, 120, 130, 140) 내부에 로딩된 보우트(300)는 상하 이송 장치(800)에 의해 튜브 하우징(200)과 밀착될 수 있다.The transfer robot 650 is located in the chamber moving unit 600, and the bow 300 moves the inside of the chamber moving unit 600 by the transfer robot 650 or the chambers 110 and 120 are moved in the chamber moving unit 600. , 130, 140, 150). When the bow 300 is loaded or unloaded from the chamber moving part 600 to each chamber 110, 120, 130, 140, 150, the chamber moving part 600 and each chamber 110, 120, 130, 140 , 150, the boat 300 positioned between the gates 300 may pass through. The boat 300 loaded through the gate 700 and loaded inside the chambers 110, 120, 130, and 140 may be in close contact with the tube housing 200 by the vertical transfer device 800.
본 실시에에 따른 보우트(300) 및 튜브 하우징(200) 중 적어도 하나는 금속으로 형성될 수 있다. 보우트(300) 및 튜브 하우징(200)은 승화 정제 장치(1000)의 내부 재질로 이루어진 부분으로, 내부 재질로 이루어진 부분은 보우트(300) 및 튜브 하우징(200) 중에서 승화 정제 대상 물질과 접촉하는 부분일 수 있다. 여기서, 금속은 티타튬, 탄탈륨, 알루미나, 스테인레스강, 텅스텐, 은, 구리, 인바, 알루미늄 등을 포함할 수 있다. 바람직하게는 티타늄 또는 탄탈륨일 수 있다. 종래에 사용하던 석영은, 일반적인 유리의 일종으로써 주성분인 이산화규소만으로 이루어져 불순물 함량이 극히 적으며, 반도체, 실험 기수 및 광학 부품 등으로 사용된다. 석영은 광투과성, 열안정성, 내화학성 및 고순도의 재질을 갖는 점에서 장점이 있으나, 내구성에 취약하고 부품 가공의 한계가 있으며 열전도율이 낮은 단점이 있다. 따라서, 석영 재질로 승화 정제 장치를 제조하게 되면, 크기 가공의 한계가 있고, 열전도율이 낮아 두께 등의 크기를 크게 하면 승화 정제를 하기 위해 가열하는 시간 등이 오래 걸리며, 분해/조립 시 작업의 불합리성 등으로 인해 정제 물질을 대량 생산하기 어렵다.At least one of the boat 300 and the tube housing 200 according to the present embodiment may be formed of metal. The bow 300 and the tube housing 200 are parts made of the inner material of the sublimation purification apparatus 1000, and the part made of the inner material is a part of the bow 300 and the tube housing 200 that comes into contact with the substance to be purified. Can be Here, the metal may include titanium, tantalum, alumina, stainless steel, tungsten, silver, copper, invar, aluminum, and the like. It may be preferably titanium or tantalum. Quartz, which has been used in the related art, is a kind of general glass, and is made of only silicon dioxide, which is a main component, and has a very low impurity content, and is used for semiconductors, laboratory equipment, and optical components. Quartz has advantages in that it has a material of light transmittance, thermal stability, chemical resistance and high purity, but it is vulnerable to durability, has limitations in processing parts, and has a disadvantage of low thermal conductivity. Therefore, if a sublimation purification device is manufactured of quartz material, there is a limitation in size processing, and if the size of the thickness is large due to low thermal conductivity, it takes a long time to heat the sublimation purification, and the irrationality of work during disassembly / assembly It is difficult to mass-produce purified substances due to the like.
보우트의 금속 재질의 예로서, 티타늄을 사용할 수 있고, 티타늄은 금속 비중이 작으면서 가볍고 단단하며, 내식성이 우수하여 변형이나 부식에 강하다. 따라서, 고강도 재질 성분을 이용하여 용융하고자 하는 물질을 효과적으로 상변화 컨트롤하고 크기 가공에 한계가 적다. 보우트의 금속 재질의 예로서, 탄탈륨을 사용할 수 있고, 탄탈륨은 연성이 뛰어나고 가공성이 용이하며, 열전도율과 전기 전도율이 매우 좋다.As an example of the metal material of the boat, titanium can be used, and titanium is light and hard with a small specific gravity of the metal, and is excellent in corrosion resistance and excellent in deformation and corrosion. Therefore, it is possible to effectively control the phase change of a material to be melted using a high-strength material component, and there is little limitation in size processing. As an example of the metal material of the boat, tantalum can be used, and tantalum is excellent in ductility, easy to process, and has very good thermal conductivity and electrical conductivity.
튜브 하우징의 금속 재질의 예로서, 역시 티타늄을 사용할 수 있고, 티타늄은 앞에서 설명한 특징을 갖기 때문에 클리닝이 용이하고 열전달이 안정하기 때문에 가열 조건을 정확히 컨트롤하여 상변화가 용이하며, 상변화된 물질이 각각의 정제존에 해당하는 챔버간의 이동이 용이할 수 있다. 튜브 하우징의 금속 재질의 예로서, 역시 탄탈륨을 사용할 수 있다.As an example of the metal material of the tube housing, titanium can also be used, and since titanium has the characteristics described above, it is easy to clean and heat transfer is stable, so it is easy to change the phase by accurately controlling the heating conditions, and each phase-changed material It may be easy to move between the chambers corresponding to the purification zone. As an example of the metallic material of the tube housing, tantalum can also be used.
본 실시예에 따른 승화 정제 장치(1000)에 포함된 제1 챔버(110) 및 제3 챔버(130)에서는 보우트(300)에 담긴 승화하고자 하는 물질에 혼합되어 있는 아웃개싱 및 기타 불순물을 제거하는 공정이 수행될 수 있다. 여기서 아웃개싱 및 기타 불순물은 승화 정제 대상 물질에 혼합되어 있는 유기 불순물일 수 있다. 아웃개싱은 승화 공정 전 단계인 합성 공정에서 사용되는 용제로서 에탄올, 수분, 헥산 등의 용매이고, 기타 불순물은 양품 분자량보다 작은 단분자 화합물 등일 수 있다.In the first chamber 110 and the third chamber 130 included in the sublimation purification apparatus 1000 according to the present embodiment, outgassing and other impurities mixed in a substance to be sublimated contained in the boat 300 are removed. The process can be performed. Here, the outgassing and other impurities may be organic impurities mixed in a sublimation purification target material. Outgassing is a solvent used in a synthesis process, which is a step prior to the sublimation process, and is a solvent such as ethanol, water, and hexane, and other impurities may be monomolecular compounds smaller than a good molecular weight.
도 3에 도시한 제1 챔버(110) 및 제3 챔버(130) 각각의 왼쪽의 보우트(300)에는 승화하고자 하는 물질이 담기고, 오른쪽의 보우트(300)에는 튜브 하우징(200)에서 가열 이후 냉각된 아웃개싱 및 기타 불순물들이 포획된다. 따라서, 1차 승화 정제된 물질은 왼쪽의 보우트(300)에 남아 있고, 1차 승화 정제된 물질이 담긴 보우트(300)가 제2 챔버(120) 및 제4 챔버(140)로 이동될 수 있다.The first chamber 110 and the third chamber 130 shown in FIG. 3 contain the substance to be sublimed in the left side 300, and the right side 300 after heating in the tube housing 200. Cooled outgassing and other impurities are captured. Therefore, the primary sublimation purified material remains on the left side of the boat 300, and the primary sublimation purified material containing the boat 300 can be moved to the second chamber 120 and the fourth chamber 140. .
제2 챔버(120) 및 제4 챔버(140) 각각의 왼쪽의 보우트(300)에는 1차 승화 정제된 물질이 담겨 있고, 이 물질이 히팅부(400)를 통과하면서 용융되어 기체화되고, 기체화된 물질이 용액화되며, 용액화된 물질이 오른쪽의 보우트(300)에 승화 정제된 물질로서 포획될 수 있다. 제2 챔버(120) 및 제4 챔버(140)의 오른쪽 보우트(300)에 포획된 승화 정제된 물질은 냉각 챔버(150)로 전달되어 냉각 과정을 거쳐 유기 발광 소자용 물질로 회수될 수 있다.The first sublimation purified material is contained in the bow 300 of each of the second chamber 120 and the fourth chamber 140, and the material is melted and gasified while passing through the heating unit 400, The liquefied material is liquefied, and the liquefied material can be captured as a sublimation purified material on the right side boat 300. Sublimation purified material captured on the right boat 300 of the second chamber 120 and the fourth chamber 140 may be transferred to the cooling chamber 150 to be recovered as a material for an organic light emitting device through a cooling process.
다시 말해, 제1 챔버(110)에 위치하는 튜브 하우징(200)은 제1 챔버(110)에 로딩된 제1 보우트에 담긴 승화 정제 대상 물질을 가열하여 제거된 불순물이 상기 제2 보우트에 포획되고, 제1 챔버(110)로부터 언로딩된 제1 보우트가 챔버 이동부(600)를 통해 제2 챔버(120)에 로딩되며, 제2 챔버(120)에 로딩된 제1 보우트에 담긴 승화 정제 대상 물질이 용융화하여 기체로 활성화되고, 기체화된 물질이 용액화되며, 용액화된 물질이 제2 보우트에 승화 정제된 물질로서 포획될 수 있다.In other words, the tube housing 200 located in the first chamber 110 heats the sublimation purification material contained in the first boat loaded in the first chamber 110 to remove impurities removed from the second boat. , The first boat unloaded from the first chamber 110 is loaded into the second chamber 120 through the chamber moving part 600, and the sublimation purification target contained in the first boat loaded in the second chamber 120 The material is melted and activated with gas, the gasified material is in solution, and the solution can be captured as a sublimated purified material in the second boat.
앞에서 설명한 제1 챔버(110) 및 제2 챔버(120) 내에서 정제 과정이 차례로 수행된 후, 제2 챔버(120)의 오른쪽 보우트(300)가 바로 냉각 챔버(150)로 이동되거나, 추가적인 승화 정제 공정이 필요한 경우에는 제1 챔버(110) 및 제2 챔버(120)에서 차례로 수행된 정제 과정이, 제3 챔버(130) 및 제4 챔버(140) 내에서 다시 한차례 반복 수행될 수도 있다.After the purification process is sequentially performed in the first chamber 110 and the second chamber 120 described above, the right boat 300 of the second chamber 120 is directly moved to the cooling chamber 150, or additional sublimation When a purification process is required, the purification process sequentially performed in the first chamber 110 and the second chamber 120 may be repeated once again in the third chamber 130 and the fourth chamber 140.
이하에서는 도 4 내지 도 7을 참고하여, 각 챔버(110, 120, 130, 140) 내부에 위치하여 승화 정제 경로와 관련된 튜브 하우징(200), 보우트(300), 히팅부(400) 및 냉각부(500)에 대해 상세히 설명하기로 한다.Hereinafter, referring to FIGS. 4 to 7, the tube housing 200, the boat 300, the heating unit 400, and the cooling unit associated with the sublimation purification path are located inside each chamber 110, 120, 130, and 140. (500) will be described in detail.
도 4는 도 3의 승화 정제 장치에서 하나의 챔버 내 위치하는 튜브 하우징과 보우트가 밀착된 형태를 확대하여 나타낸 도면이다. 도 5는 도 4의 승화 정제 장치에서 튜브 하우징 일부가 틸트된 구조를 갖는 변형 실시예를 나타내는 도면이다. 도 6은 도 3의 승화 정제 장치에서 챔버 내부로 보우트가 로딩되는 모습을 나타내는 도면이다. 도 7은 도 4에서 튜브 하우징과 보우트가 밀착된 모습을 나타내는 사시도이다.FIG. 4 is an enlarged view of a tube housing and a boat positioned in one chamber in a sublimation purification apparatus of FIG. 3 in close contact. FIG. 5 is a view showing a modified embodiment in which a part of the tube housing has a tilted structure in the sublimation purification device of FIG. 4. FIG. 6 is a view showing a state in which the boat is loaded into the chamber in the sublimation purification apparatus of FIG. 3. 7 is a perspective view showing a state in which the tube housing and the boat are in close contact in FIG. 4.
도 4를 참고하면, 본 실시예에서 튜브 하우징(200)은 제1 보우트(300a)에 담긴 승화 정제 대상 물질이 가열된 이후 제2 보우트(300b)에 포획되도록 하는 승화 정제 대상 물질의 이동 경로가 될 수 있다. 승화 정제 대상 물질은 유기물 및 불순물이 혼합된 혼합 재료일 수 있다.Referring to FIG. 4, in this embodiment, the tube housing 200 has a movement path of a sublimation purification target material to be captured in the second boat 300b after the sublimation purification target material contained in the first boat 300a is heated. Can be. Substances subject to sublimation purification may be mixed materials in which organic substances and impurities are mixed.
본 실시예에 따른 튜브 하우징(200) 바깥면에 인접하여 위치하는 히팅부(400)는 제1 보우트(300a)에 대응하는 부분에 위치하는 제1 히팅존(410), 제1 보우트(300a)와 제2 보우트(300b) 사이에 위치하는 제2 히팅존(420) 및 제2 보우트(300b)에 대응하는 부분에 위치하는 제3 히팅존(430)을 포함한다. 제1 보우트(300a)에 담긴 승화 정제 대상 물질이 제1 보우트(300a) 하부에 위치하는 하부 히팅부(440)에 의해 가열되어 용액화되고, 추가로 온도를 상승시켜 승화 정제 대상 물질은 기체로 활성화되며, 기체로 활성화된 승화 물질이 튜브 하우징(200)의 제1 제1 히팅존(410)에 도달한 후 온도가 낮은 제2 히팅존(420)으로 이동한다. 이때, 제1 히팅존(410)은 제1 보우트(300a)와 동등한 온도 조건을 유지함으로써 기체 상태를 유지하며, 기체 상태의 승화 물질이 제2 히팅존(420)으로 날아가도록 한다.The heating part 400 positioned adjacent to the outer surface of the tube housing 200 according to the present embodiment includes a first heating zone 410 and a first boat 300a located in a portion corresponding to the first boat 300a. And a second heating zone 420 positioned between the second boat 300b and a third heating zone 430 positioned at a portion corresponding to the second boat 300b. Sublimation purification target material contained in the first boat 300a is heated and liquefied by the lower heating unit 440 located under the first boat 300a, and the temperature of the sublimation purification target is further increased by gas. Activated, the gas-activated sublimation material reaches the first first heating zone 410 of the tube housing 200 and then moves to the second heating zone 420 having a low temperature. At this time, the first heating zone 410 maintains a gas state by maintaining a temperature condition equivalent to that of the first boat 300a, and allows the sublimation material in the gas state to fly to the second heating zone 420.
제2 히팅존(420)은 온도를 낮추어 상기 기체로 활성화된 승화 정제 대상 물질을 액체 상태로 상변화시킬 수 있다. 이때, 제1 히팅존(410)의 과도한 열간섭으로 인해 물질간 상변화를 컨트롤하기 위해 제2 히팅존(420)은 냉각 기능도 함께 가질 수 있다. 제2 히팅존(420)에서 액상화된 물질이 제3 히팅존(430)으로 들어가게 되고, 제3 히팅존(430)은 온도를 컨트롤하여 상기 용액화된 승화 정제 대상 물질의 용액 상태의 온도를 유지할 수 있도록 한다. 제3 히팅존(430)을 거쳐 승화 정제 대상 물질은 제2 보우트(300b)에 용액 상태로 떨어지게 된다. 이때, 변형 실시예로서, 도 5에 도시한 바와 같이 튜브 하우징(200)은, 승화 정제 대상 물질의 이동 경로를 따라 틸트된 구조를 가질 수 있다. 틸트된 구조로 인해 제1 보우트(300a)에서 제2 보우트(300b)로 물질의 이동이 원활하게 이루어질 수 있다. 틸트는 구조는 용액화된 승화 정제 대상 물질이 제2 보우트(300b)로 잘 흐르도록 하기 위한 것이다. 틸트된 정도는 대략 5도일 수 있다.The second heating zone 420 may lower the temperature to phase change the sublimation purification target material activated with the gas into a liquid state. At this time, the second heating zone 420 may also have a cooling function in order to control phase changes between materials due to excessive heat interference of the first heating zone 410. The material liquefied in the second heating zone 420 enters the third heating zone 430, and the third heating zone 430 controls the temperature to maintain the temperature of the solution state of the sublimated purification target material. Make it possible. Substances subject to sublimation purification through the third heating zone 430 are dropped into a solution state in the second boat 300b. At this time, as a modified embodiment, as shown in FIG. 5, the tube housing 200 may have a tilted structure along a movement path of a sublimation purification target material. Due to the tilted structure, the material can be smoothly moved from the first boat 300a to the second boat 300b. The structure of the tilt is to allow the material to be purified to be sublimated to flow well to the second boat 300b. The tilted degree may be approximately 5 degrees.
도 6을 참고하면, 도 3에서의 게이트(700)를 통과하여 챔버(120) 내부에 로딩된 보우트(300)는 상하 이송 장치(800)에 의해 튜브 하우징(200)과 밀착될 수 있다. 상하 이송 장치(800)는 로딩된 보우트(300)를 챔버(120) 내에 위치하는 튜브 하우징(200)에 밀착하여 승화 정제 공정이 수행될 수 있도록 챔버(120) 내에서 보우트(300)를 이동시키는 역할을 할 수 있다.Referring to FIG. 6, the boat 300 loaded through the gate 700 in FIG. 3 and loaded inside the chamber 120 may be in close contact with the tube housing 200 by the vertical transfer device 800. The vertical transfer device 800 moves the boat 300 in the chamber 120 so that the loaded boat 300 is in close contact with the tube housing 200 located in the chamber 120 so that a sublimation purification process can be performed. Can play a role.
상하 이송 장치(800)는 공압 실런더일 수 있다. 제1 보우트(300a) 아래 탑재되어 있는 하부 히팅부(440, 450)가 상하 이송 장치(800)에 의해 하부로 내려가 있는 상태에서 도 3에서 설명한 이송 로봇(650)이 제1 보우트(300a)를 제2 챔버(120)에 장착할 수 있다. 이후, 게이트를 닫고 진공 분위기를 조성한 상태에서, 상하 이송 장치(800)를 이용하여 하부 히팅부(440, 450)를 튜브 하우징(200) 쪽으로 올려줌으로써, 제2 챔버(120)에 장착된 제1 보우트(300a)가 튜브 하우징(200)에 물리적인 힘에 의해 밀착하여 결합될 수 있다. 제1 보우트(300a)와 튜브 하우징(200)이 밀착/결합됨으로써 기체화된 물질이 제1 보우트(300a)와 튜브 하우징(200)의 틈새로 유실되어 발생할 수 있는 외부 오염을 방지할 수 있다.The vertical transfer device 800 may be a pneumatic sealer. The transfer robot 650 described in FIG. 3 moves the first boat 300a while the lower heating units 440 and 450 mounted below the first boat 300a are lowered by the vertical transfer device 800. It can be mounted on the second chamber 120. Subsequently, by closing the gate and creating a vacuum atmosphere, the lower heating units 440 and 450 are raised toward the tube housing 200 by using the up-and-down transfer device 800, so that the first mounted in the second chamber 120 is mounted. The boat 300a may be tightly coupled to the tube housing 200 by physical force. Since the first boat 300a and the tube housing 200 are in close contact / combination, it is possible to prevent external contamination that may occur due to the gasified material being lost into the gap between the first boat 300a and the tube housing 200.
이에 반해, 제2 보우트(300b)는 튜브 하우징(200)과 분리된 상태로 존재하여, 제1 보우트(300a)와 튜브 하우징(200)이 밀착 결합된 상태로 유지되면서 승화가 이루어지고, 이때 튜브 하우징(200)과 분리된 상태에서 제2 보우트(300b)는 액상화된 물질을 모아둔다. 구체적으로, 튜브 하우징(200)의 틸트 구조에 따른 기울어진 각도에 의해 액상화된 물질이 위에서 아래로 떨어지는 현상을 통해 제2 보우트(300b)에 모아질 수 있다. 또한, 튜브 하우징(200)과 제2 보우트(300b)가 분리되어 있음으로 인해 제2 챔버(120)의 내부 압력과 튜브 하우징(200)의 내부 압력이 동일하게 유지될 수 있다.On the other hand, the second boat 300b exists in a separate state from the tube housing 200, so that the sublimation is performed while the first boat 300a and the tube housing 200 are kept in close contact with each other. In the state separated from the housing 200, the second boat 300b collects the liquefied material. Specifically, the material liquefied by the inclined angle according to the tilt structure of the tube housing 200 may be collected in the second boat 300b through the phenomenon of falling from top to bottom. In addition, because the tube housing 200 and the second boat 300b are separated, the internal pressure of the second chamber 120 and the internal pressure of the tube housing 200 may be maintained the same.
도 7을 참고하면, 본 실시예에 따른 승화 정제 장치는 보우트(300)와 튜브 하우징(200)이 밀착되는 경우, 보우트(300)와 튜브 하우징(200) 사이에 개재되어 있는 실링 가스켓(250)을 더 포함할 수 있다. 실링 가스켓(250)은 튜브 하우징(200)의 단부에 형성되어 있고, 실링 가스켓(250)은 튜브 하우징(200)의 단부가 꺾인 부분에 발생하는 좁은 틈을 채우고 있다. 실링 가스켓(250)은 티타늄(Ti), 은(Ag), 구리(Cu) 및 세라믹 중 적어도 하나를 포함할 수 있다.Referring to FIG. 7, in the sublimation purification apparatus according to the present embodiment, when the bow 300 and the tube housing 200 are in close contact, the sealing gasket 250 is interposed between the bow 300 and the tube housing 200. It may further include. The sealing gasket 250 is formed at the end of the tube housing 200, and the sealing gasket 250 fills a narrow gap occurring in a portion where the end of the tube housing 200 is bent. The sealing gasket 250 may include at least one of titanium (Ti), silver (Ag), copper (Cu), and ceramic.
실링 가스켓(250)은 챔버(120) 내에서 고체를 가열하면 유체가 되는데, 이러한 유체가 튜브 하우징 밖으로 새어 나오는 것을 방지할 수 있다.The sealing gasket 250 becomes a fluid when the solid is heated in the chamber 120, and this fluid can be prevented from leaking out of the tube housing.
이하에서는 도 8을 참고하여 히팅부에 대해 구체적으로 설명하기로 한다. 도 8은 본 발명의 일 실시예에 따른 히팅부를 나타내는 사시도이다.Hereinafter, the heating unit will be described in detail with reference to FIG. 8. 8 is a perspective view showing a heating unit according to an embodiment of the present invention.
도 8을 참고하면, 튜브 하우징(200)이 욕조 모양을 갖고, 욕조가 뒤집힌 구조를 가질 수 있다. 튜브 하우징(200)의 양 가장자리에 각각 제1 보우트(300a)와 제2 보우트(300b)가 밀착되어 있다.Referring to FIG. 8, the tube housing 200 may have a tub shape, and the tub may have an inverted structure. The first boat 300a and the second boat 300b are in close contact with both edges of the tube housing 200, respectively.
본 실시예에 따른 히팅부는 튜브 하우징(200)의 바깥면에 인접하여 위치하는 상부 히팅부와, 제1, 2 보우트(300a, 300b)의 바깥면에 인접하여 위치하는 하부 히팅부를 포함한다. 상기 상부 히팅부는 제1 보우트(300a)에 대응하는 부분에 위치하는 제1 히팅존(410), 제1 보우트(300a)와 제2 보우트(300b) 사이에 위치하는 제2 히팅존(420) 및 제2 보우트(300b)에 대응하는 부분에 위치하는 제3 히팅존(430)을 포함한다. 상기 하부 히팅부는 제1 보우트(300a)의 측면을 감싸는 제4 히팅존(440)과 제2 보우트(300b)의 측면을 감싸는 제5 히팅존(450)을 포함한다.The heating unit according to the present embodiment includes an upper heating unit positioned adjacent to the outer surface of the tube housing 200 and a lower heating unit positioned adjacent to the outer surfaces of the first and second boats 300a and 300b. The upper heating part includes a first heating zone 410 positioned in a portion corresponding to the first boat 300a, a second heating zone 420 positioned between the first boat 300a and the second boat 300b, and It includes a third heating zone 430 located in the portion corresponding to the second boat (300b). The lower heating part includes a fourth heating zone 440 surrounding the side surface of the first boat 300a and a fifth heating zone 450 surrounding the side surface of the second boat 300b.
본 실시예에 따른 히팅부는 탄탈륨으로 형성할 수 있다. 탄탈륨은 연성이 뛰어나고 가공성이 용이하며, 열전도율과 전기 전도율이 좋기 때문에 가열하고자 하는 히팅존에서 독립된 열전달이 가능하고, 열전달 컨트롤이 매우 안정적일 수 있다. 또는, 히팅부가 인코넬(Inconel)로 형성될 수 있다. 인코넬은 내열성이 좋고 대략 섭씨 900도 이상의 산화 조건에서도 산화하지 않고 신장, 인장강도, 항복점 등 여러 성질도 섭씨 600도까지 변하지 않는 우수한 성질을 가질 수 있다.The heating unit according to the present embodiment may be formed of tantalum. Since tantalum is excellent in ductility, easy to process, and has good thermal conductivity and electrical conductivity, independent heat transfer is possible in the heating zone to be heated, and heat transfer control can be very stable. Alternatively, the heating portion may be formed of Inconel. Inconel has good heat resistance and does not oxidize even in an oxidizing condition of about 900 degrees Celsius or higher, and may have excellent properties such as elongation, tensile strength, and yield point that do not change up to 600 degrees Celsius.
도 9는 본 발명의 다른 일 실시예에 따른 승화 정제 장치의 한 챔버 내에서 보우트가 튜브 하우징에 밀착된 상태를 나타내는 도면이다. 도 10은 도 9의 A부분에서 상하 이송 장치와 승화 정제량 측정 부재를 나타내는 사시도이다. 도 11은 도 10의 승화 정제량 측정 부재를 나타내는 정면도이다.9 is a view showing a state in which the boat is in close contact with the tube housing in one chamber of the sublimation purification apparatus according to another embodiment of the present invention. 10 is a perspective view showing a vertical transfer device and a sublimation purification amount measuring member in part A of FIG. 9. 11 is a front view showing the sublimation purification amount measuring member of FIG. 10.
도 9 및 도 10을 참고하면, 본 실시예에 따른 승화 정제 장치는 챔버(120) 내부에 고정되어 있는 승화 정제량 측정 부재(850)를 더 포함한다. 승화 정제량 측정 부재(850)는 보우트(300)의 하부에 위치할 수 있다. 이처럼 보우트(300) 하부에 승화 정제량 측정 부재(850)가 위치함으로써, 승화 정제 공정 진행 중에 실시간으로 승화 정제량을 확인할 수 있다. 승화 정제량 측정 부재(850)는 하중 센서로서 힘 또는 하중을 측정하기 위한 변환기이며, 출력을 전기적 신호로 출력할 수 있는 장치이다.9 and 10, the sublimation purification apparatus according to the present embodiment further includes a sublimation purification amount measuring member 850 fixed inside the chamber 120. The sublimation purification amount measuring member 850 may be located under the boat 300. As such, the sublimation purification amount measurement member 850 is located at the bottom of the boat 300, so that the sublimation purification amount can be checked in real time during the sublimation purification process. The sublimation purification amount measuring member 850 is a transducer for measuring force or load as a load sensor, and is a device capable of outputting an output as an electrical signal.
구체적으로 도 11을 참고하면, 보우트(300) 하단에 위치하는 가열부인 히팅부(440)는 보우트(300)를 감싸고 있으나, 본 실시예에 따른 승화 정제량 측정 부재(850)는 히팅부(440) 하단 중앙부에서 히팅부(440)에 간섭되지 않는 부분에 삼발이 형태의 핀(860)이 돌출되어 있다. 히팅부(440)는 와이어 타입의 열선일 수 있는데, 열선은 간격을 가지면서 복수로 형성되어 도 9에서와 같이 튜브 하우징(200)을 전체적으로 감싸고 있는 형태이다. 다시 말해, 복수의 열선 사이에서 삼발이 형태의 핀(860)이 상부 방향으로 돌출되기 때문에 히팅부(440)의 간섭 없이 보우트(300)와 승화 정제량 측정 부재(850)가 조립될 수 있다.Specifically, referring to FIG. 11, the heating part 440, which is a heating part located at the bottom of the bow 300, surrounds the bow 300, but the sublimation purification amount measuring member 850 according to this embodiment has a heating part 440. ) In the lower center portion, a tripod-shaped pin 860 protrudes from a portion that does not interfere with the heating portion 440. The heating unit 440 may be a wire-type heating wire, and the heating wire is formed in a plurality while having a gap, thereby enclosing the tube housing 200 as shown in FIG. 9. In other words, between the plurality of heating wires, the tripod-shaped pin 860 protrudes upward, so that the boat 300 and the sublimation purification amount measuring member 850 can be assembled without interference from the heating unit 440.
보우트(300)를 받치고 있는 상하 이송 장치(800)에 의해 보우트(300)가 하부로 이동하면, 승화 정제량 측정 부재(850)의 핀(860)에 보우트(300)가 도달하게 된다. 이때, 보우트(300) 안의 승화 정제 물질의 정제량을 측정할 수 있다.When the boat 300 moves downward by the vertical transfer device 800 supporting the boat 300, the boat 300 reaches the pin 860 of the sublimation purification amount measuring member 850. At this time, the purification amount of the sublimation purification material in the boat 300 can be measured.
기존에는 단순히 승화 정제량을 육안으로 확인한 후, 경험에 의한 주관적 시각으로 공정 조건 및 공정 종료 시점을 판단할 수 있었다면, 본 실시예에 따른 승화 정제 장치는, 승화 정제량 측정 부재(850)를 사용하여 물질 이동량 및 물질 소모량을 공정 중에 실시간으로 확인할 수 있기 때문에 공정간 편차 및 공정상 발생할 수 있는 문제를 최소화할 수 있다.In the past, if the sublimation purification amount was simply visually confirmed, and the process conditions and the process termination time could be determined from a subjective viewpoint based on experience, the sublimation purification device according to the present embodiment uses a sublimation purification amount measurement member 850 Therefore, it is possible to check the material movement amount and material consumption in real time during the process, thereby minimizing the deviation between processes and problems that may occur in the process.
이하에서는 도 3 내지 도 8을 다시 참조하여, 본 발명의 다른 일 실시예에 따른 승화 정제 방법에 대해 설명하기로 한다.Hereinafter, a method of sublimation purification according to another embodiment of the present invention will be described with reference to FIGS. 3 to 8 again.
도 3 내지 도 8을 참고하면, 본 실시예에 따른 승화 정제 방법은, 제1 챔버(110)에 승화 정제 대상 물질을 담은 제1 보우트(300a)를 로딩한 후 가열하여 승화 정제 대상 물질에 혼입되어 있는 아웃개싱 및 기타 불순물을 1차 제거한다. 이때, 정제된 물질 외에 잔류 용매 및 단분자 불순물들이 1차 승화되어 제2 보우트(300b)에 포획된다. 이후 승화되지 않는 온도 즉, 기체화되지 않는 범위의 온도까지 냉각한다.3 to 8, in the sublimation purification method according to the present embodiment, the first chamber 300 loaded with the sublimation purification target material in the first chamber 110 is loaded and heated to be mixed with the sublimation purification target material Outgassing and other impurities are removed first. At this time, in addition to the purified material, residual solvent and monomolecular impurities are first sublimed and trapped in the second boat 300b. Thereafter, the temperature is not sublimated, that is, cooled to a temperature in a range that is not gasified.
이후 제1 챔버(110)에서 1차 정제된 물질이 담긴 제1 보우트(300a)를 제1 챔버(110)로부터 언로딩하여 이송 로봇(650)을 통해 제2 챔버(120)에 제1 보우트(300a)를 로딩한다. 제2 챔버(120)에 로딩된 제1 보우트(300a)에 담긴 승화 정제 대상 물질을 제4 히팅존(440)으로 가열하여 용액화하고, 추가로 온도를 상승시켜 기체로 활성화시킨다. 기체로 활성화된 승화 물질이 제1 히팅존(410)으로 이동하며, 제1 히팅존(410)에서 제1 보우트(300a)와 동등한 온도를 유지함으로써 기체로 활성화된 승화 물질이 제2 히팅존(420)으로 날아가도록 한다. 제2 히팅존(420)에서 온도를 낮추어 상기 기체로 활성화된 승화 정제 대상 물질을 용액화한다. 제2 히팅존(420)에서 용액화된 물질이 제3 히팅존(430)으로 들어가고, 제3 히팅존(430)을 컨트롤하여 상기 용액화된 승화 정제 대상 물질의 용액 상태의 온도를 유지하여 제2 보우트(300b)에 용액 상태로 떨어뜨려 포획한다. 제2 챔버(120)에서 공정이 완료된 후, 제2 보우트(300b)를 이송 로봇(650)을 사용하여 냉각 챔버(150)로 이동하고, 냉각 챔버(150)에 로딩된 제2 보우트(300b)에 담긴 상기 용액화된 물질을 냉각시킬 수 있다.Subsequently, the first boat 300a containing the first purified material in the first chamber 110 is unloaded from the first chamber 110, and the first boat is transferred to the second chamber 120 through the transfer robot 650 ( 300a). The sublimation purification target material contained in the first boat 300a loaded in the second chamber 120 is heated to a fourth heating zone 440 to be solutiond, and the temperature is further increased to activate the gas. The sublimation material activated by gas moves to the first heating zone 410, and the sublimation material activated by gas maintains the same temperature as the first boat 300a in the first heating zone 410 so that the sublimation material activated by gas is the second heating zone ( 420). By lowering the temperature in the second heating zone 420, the sublimation purification target material activated with the gas is solutiond. The substance liquefied in the second heating zone 420 enters the third heating zone 430, and controls the third heating zone 430 to maintain the temperature of the solution state of the solution-sublimed purification target material. 2 Drop to the boat (300b) in a solution state and capture. After the process is completed in the second chamber 120, the second boat 300b is moved to the cooling chamber 150 using the transfer robot 650, and the second boat 300b loaded in the cooling chamber 150 The solution material contained in can be cooled.
상기 승화 정제 공정 중에, 냉각 챔버(150)로 제2 보우트(300b)를 로딩시키기 전에 고순도의 정제 물질을 얻기 위해, 제1 챔버(110)와 제2 챔버(120)에서 순차적으로 진행한 공정을, 제3 챔버(130)와 제4 챔버(140)에서 동일하게 반복 수행할 수 있다.During the sublimation purification process, in order to obtain a high-purity purification material before loading the second boat 300b into the cooling chamber 150, a process sequentially performed in the first chamber 110 and the second chamber 120 is performed. , It may be repeatedly performed in the third chamber 130 and the fourth chamber 140.
제1 보우트(300a), 제2 보우트(300b) 및 튜브 하우징(200)은 금속으로 형성되고, 본 실시예에 따른 승화 정제 방법은 상기 금속으로 형성된 부품을 화학 용액 세정하는 단계를 더 포함할 수 있다. 이러한 세정 공정을 통해, 고진공시 히팅부와 보우트 및 튜브 하우징을 이루는 금속 성분 물질에서 용출되는 금속 불순물이 승화 정제 대상 물질에 혼입되어 유기 발광 소자 제소시 전압 상승 및 수명 단축 등의 문제를 방지할 수 있다.The first boat 300a, the second boat 300b, and the tube housing 200 are formed of metal, and the sublimation purification method according to the present embodiment may further include cleaning a chemical solution of parts formed of the metal. have. Through such a cleaning process, metal impurities eluted from the metal component material constituting the heating part, the boat, and the tube housing during high vacuum are mixed in the sublimation purification target material, thereby preventing problems such as an increase in voltage and a shortened lifespan when filing an organic light emitting device. have.
추가로, 본 실시예에 따른 승화 정제 방법은 상기 세정하는 단계 이후에 베이킹하는 단계를 더 포함할 수 있다. 베이킹하는 단계는 대략 섭씨 200도 이상의 온도에서 수행될 수 있고, 적어도 2회 수행될 수 있다.Additionally, the sublimation purification method according to the present embodiment may further include baking after the washing step. Baking may be performed at a temperature of about 200 degrees Celsius or higher, and may be performed at least twice.
이상에서 본 발명의 바람직한 실시예에 대하여 상세하게 설명하였지만 본 발명의 권리범위는 이에 한정되는 것은 아니고 다음의 청구범위에서 정의하고 있는 본 발명의 기본 개념을 이용한 당업자의 여러 변형 및 개량 형태 또한 본 발명의 권리범위에 속하는 것이다.The preferred embodiments of the present invention have been described in detail above, but the scope of the present invention is not limited to this, and various modifications and improvements of those skilled in the art using the basic concept of the present invention defined in the following claims are also provided. It belongs to the scope of rights.
[부호의 설명][Description of codes]
1000: 승화 정제 장치1000: sublimation purification device
110, 120, 130, 140: 챔버110, 120, 130, 140: chamber
150: 냉각 챔버150: cooling chamber
200: 튜브 하우징200: tube housing
250: 실링 가스켓250: sealing gasket
300: 보우트300: boat
400: 히팅부400: heating section
410, 420, 430, 440, 450: 히팅존410, 420, 430, 440, 450: heating zone
500: 냉각부500: cooling unit
600: 챔버 이동부600: chamber moving part
650: 이송 로봇650: transfer robot
700: 게이트700: gate
800: 상하 이송 장치800: up and down transfer device
850: 승화 정제량 측정 부재850: no sublimation purification amount measurement

Claims (24)

  1. 진공 챔버,Vacuum Chamber,
    상기 진공 챔버 내에 위치하는 튜브 하우징,A tube housing located in the vacuum chamber,
    상기 튜브 하우징에 밀착되어 있는 보우트 그리고A bolt in close contact with the tube housing and
    상기 보우트의 바깥면 및 상기 튜브 하우징 바깥면에 인접하여 위치하는 히팅부를 포함하고,And a heating portion located adjacent to the outer surface of the boat and the outer surface of the tube housing,
    상기 보우트에 승화 정제 대상 물질이 담기고, 상기 보우트 및 상기 튜브 하우징 중 적어도 하나는 금속으로 형성된 승화 정제 장치.The sublimation purification target material is contained in the boat, and at least one of the boat and the tube housing is formed of a metal.
  2. 제1항에서,In claim 1,
    상기 보우트는 제1 보우트 및 제2 보우트를 포함하고, 상기 제1 보우트와 상기 제2 보우트는 상기 진공 챔버 내에 함께 위치하고, 상기 튜브 하우징이 이동 경로가 되어 상기 제1 보우트에 담긴 승화 정제 대상 물질이 가열된 이후 상기 제2 보우트에 포획되도록 하는 승화 정제 장치.The boat includes a first boat and a second boat, and the first boat and the second boat are located together in the vacuum chamber, and the tube housing becomes a movement path, whereby the sublimation purification material contained in the first boat is Sublimation purification device to be trapped in the second boat after being heated.
  3. 제2항에서,In claim 2,
    상기 튜브 하우징 바깥면에 인접하여 위치하는 히팅부는 상기 제1 보우트에 대응하는 부분에 위치하는 제1 히팅존, 상기 제1 보우트와 상기 제2 보우트 사이에 위치하는 제2 히팅존 및 상기 제2 보우트에 대응하는 부분에 위치하는 제3 히팅존을 포함하고,The heating unit located adjacent to the outer surface of the tube housing is a first heating zone positioned at a portion corresponding to the first boat, a second heating zone located between the first boat and the second boat, and the second boat It includes a third heating zone located in the portion corresponding to,
    상기 제1 히팅존은 상기 제1 보우트에 담겨 기체로 활성화된 승화 정제 대상 물질이 기체 상태를 유지하도록 온도를 컨트롤하고, 상기 제2 히팅존은 상기 기체로 활성화된 승화 정제 대상 물질을 용액화하며, 상기 제3 히팅존은 상기 용액화된 승화 정제 대상 물질의 용액 상태를 유지하도록 온도를 컨트롤하여 상기 제2 보우트에 용액 상태의 승화 정제 대상 물질이 떨어지도록 하는 승화 정제 장치.The first heating zone controls the temperature so that the sublimation purification target material activated by the gas contained in the first boat maintains a gas state, and the second heating zone liquefies the sublimation purification target material activated by the gas. , The third heating zone is a sublimation purification apparatus that controls the temperature to maintain the solution state of the solution sublimation purification target substance so that the sublimation purification target substance in solution state falls to the second boat.
  4. 제3항에서,In claim 3,
    상기 튜브 하우징은 상기 승화 정제 대상 물질의 이동 경로를 따라 틸트된 구조를 갖는 승화 정제 장치.The tube housing is a sublimation purification device having a tilted structure along a movement path of the sublimation purification target material.
  5. 제1항에서,In claim 1,
    상기 금속은 티타늄 또는 탄탈륨을 포함하는 승화 정제 장치.The metal sublimation purification apparatus comprising titanium or tantalum.
  6. 제1항에서,In claim 1,
    상기 튜브 하우징의 단부에 형성된 실링 가스켓을 더 포함하고, 상기 튜브 하우징과 상기 보우트 사이에 상기 실링 가스켓이 개재되어 있는 승화 정제 장치.A sublimation purification device further comprising a sealing gasket formed at an end of the tube housing, wherein the sealing gasket is interposed between the tube housing and the boat.
  7. 제6항에서,In claim 6,
    상기 실링 가스켓은 티타늄(Ti), 은(Ag), 구리(Cu) 및 세라믹 중 적어도 하나를 포함하는 승화 정제 장치.The sealing gasket is a sublimation purification apparatus including at least one of titanium (Ti), silver (Ag), copper (Cu), and ceramic.
  8. 챔버 이동부,Chamber moving part,
    상기 챔버 이동부에 인접하여 위치하는 복수의 챔버,A plurality of chambers located adjacent to the chamber moving portion,
    상기 챔버 내에 위치하는 튜브 하우징,A tube housing located within the chamber,
    상기 챔버 이동부와 상기 챔버들 사이에 위치하는 게이트,A gate located between the chamber moving part and the chambers,
    이송 로봇에 의해 상기 챔버 이동부 내부를 이동하거나 상기 챔버 이동부에서 상기 챔버 내부로 로딩 또는 언로딩되는 보우트 그리고A boat that moves inside the chamber moving part by a transfer robot or is loaded or unloaded from the chamber moving part into the chamber and
    상기 보우트의 바깥면 및 상기 튜브 하우징 바깥면을 둘러싸는 히팅부를 포함하고,And a heating part surrounding the outer surface of the boat and the outer surface of the tube housing,
    상기 보우트는 상기 튜브 하우징으로 서로 연결되는 제1 보우트와 제2 보우트를 포함하는 승화 정제 장치.The boat is a sublimation purification apparatus including a first boat and a second boat connected to each other with the tube housing.
  9. 제8항에서,In claim 8,
    상기 튜브 하우징 바깥면에 인접하여 위치하는 히팅부는 상기 제1 보우트에 대응하는 부분에 위치하는 제1 히팅존, 상기 제1 보우트와 상기 제2 보우트 사이에 위치하는 제2 히팅존 및 상기 제2 보우트에 대응하는 부분에 위치하는 제3 히팅존을 포함하고,The heating unit located adjacent to the outer surface of the tube housing is a first heating zone positioned at a portion corresponding to the first boat, a second heating zone located between the first boat and the second boat, and the second boat It includes a third heating zone located in the portion corresponding to,
    상기 제1 히팅존은 상기 제1 보우트에 담겨 기체로 활성화된 승화 정제 대상 물질이 기체 상태를 유지하도록 온도를 컨트롤하고, 상기 제2 히팅존은 상기 기체로 활성화된 승화 정제 대상 물질을 용액화하며, 상기 제3 히팅존은 상기 용액화된 승화 정제 대상 물질의 용액 상태를 유지하도록 온도를 컨트롤하여 상기 제2 보우트에 용액 상태의 승화 정제 대상 물질이 떨어지도록 하는 승화 정제 장치.The first heating zone controls the temperature so that the sublimation purification target material activated by the gas contained in the first boat maintains a gas state, and the second heating zone liquefies the sublimation purification target material activated by the gas. , The third heating zone is a sublimation purification apparatus that controls the temperature to maintain the solution state of the solution sublimation purification target substance so that the sublimation purification target substance in solution state falls to the second boat.
  10. 제9항에서,In claim 9,
    상기 튜브 하우징은 상기 승화 정제 대상 물질의 이동 경로를 따라 틸트된 구조를 갖는 승화 정제 장치.The tube housing is a sublimation purification device having a tilted structure along a movement path of the sublimation purification target material.
  11. 제10항에서,In claim 10,
    상기 제1 보우트와 상기 제2 보우트 중 적어도 하나는 상기 게이트를 통과한 보우트를 상기 챔버 내에서 이동시켜 상기 튜브 하우징과 밀착되도록 하는 상하 이송 장치를 더 포함하는 승화 정제 장치.At least one of the first boat and the second boat further comprises a vertical transfer device that moves the boat passing through the gate in the chamber to be in close contact with the tube housing.
  12. 제8항에서,In claim 8,
    상기 보우트 및 상기 튜브 하우징 중 적어도 하나는 금속으로 형성된 승화 정제 장치.At least one of the boat and the tube housing is a sublimation purification device formed of a metal.
  13. 제12항에서,In claim 12,
    상기 금속은 티타늄 또는 탄탈륨을 포함하는 승화 정제 장치.The metal sublimation purification apparatus comprising titanium or tantalum.
  14. 제8항에서,In claim 8,
    상기 튜브 하우징의 단부에 형성된 실링 가스켓을 더 포함하고, 상기 보우트가 상기 챔버 내부로 로딩되어 상기 튜브 하우징과 맞물릴 때, 상기 보우트와 상기 튜브 하우징 사이에 상기 실링 가스켓이 개재되는 승화 정제 장치.A sublimation purification device further comprising a sealing gasket formed at an end of the tube housing, wherein the sealing gasket is interposed between the boat and the tube housing when the boat is loaded into the chamber and engaged with the tube housing.
  15. 제8항에서,In claim 8,
    상기 복수의 챔버는 서로 이웃하는 제1 챔버와 제2 챔버를 포함하고,The plurality of chambers include a first chamber and a second chamber adjacent to each other,
    상기 제1 챔버에 위치하는 튜브 하우징은 상기 제1 챔버에 로딩된 제1 보우트에 담긴 승화 정제 대상 물질을 가열하여 제거된 불순물이 상기 제2 보우트에 포획되고, 상기 제1 챔버로부터 언로딩된 제1 보우트가 상기 챔버 이동부를 통해 상기 제2 챔버에 로딩되며, 상기 제2 챔버에 로딩된 제1 보우트에 담긴 승화 정제 대상 물질이 용융화하여 기체로 활성화되는 승화 정제 장치.In the tube housing positioned in the first chamber, impurities removed by heating a sublimation purification material contained in the first boat loaded in the first chamber are trapped in the second boat, and unloaded from the first chamber. A sublimation purification apparatus in which one boat is loaded into the second chamber through the chamber moving part, and a sublimation purification target material contained in the first boat loaded in the second chamber is melted and activated with gas.
  16. 제1 챔버 내에 승화 정제 대상 물질이 담긴 제1 보우트를 로딩하는 단계,Loading the first boat containing the sublimation purification target material in the first chamber,
    상기 로딩된 제1 보우트에 담긴 상기 승화 정제 대상 물질을 가열하여 제거된 불순물을 튜브 하우징을 통해 제2 보우트에 포획하는 단계,Capturing impurities removed by heating the sublimation purification target material contained in the loaded first boat through a tube housing to a second boat,
    상기 제1 챔버로부터 상기 제1 보우트를 언로딩하여 이송 로봇을 통해 제2 챔버에 상기 제1 보우트를 로딩하는 단계,Unloading the first boat from the first chamber and loading the first boat into the second chamber through a transfer robot,
    상기 제2 챔버에 로딩된 제1 보우트에 담긴 상기 승화 정제 대상 물질을 용융화하여 기체로 활성화시키는 단계,Melting the sublimation purification target material contained in the first boat loaded in the second chamber to activate it with a gas,
    상기 기체로 활성화된 물질을 용액화하는 단계,Solution of the substance activated with the gas,
    상기 용액화된 물질을 상기 제2 챔버에 포함된 튜브 하우징을 통해 상기 제2 챔버 내에 위치하는 제2 보우트에 포획하는 단계,Capturing the liquefied material through a tube housing included in the second chamber to a second boat located in the second chamber,
    상기 제2 챔버 내에 위치하는 상기 제2 보우트를 상기 이송 로봇을 사용하여 냉각 챔버로 이동하는 단계 그리고Moving the second boat located in the second chamber to a cooling chamber using the transfer robot; and
    상기 냉각 챔버에 로딩된 상기 제2 보우트에 담긴 상기 용액화된 물질을 냉각하는 단계를 포함하고,Cooling the liquefied material contained in the second boat loaded in the cooling chamber,
    상기 제1 보우트, 상기 제2 보우트 및 상기 튜브 하우징 중 적어도 하나는 금속으로 형성된 승화 정제 방법.At least one of the first boat, the second boat and the tube housing is a sublimation purification method formed of a metal.
  17. 제16항에서,In claim 16,
    상기 제1 보우트, 상기 제2 보우트 및 상기 튜브 하우징 중 금속으로 형성된 부품을 화학 용액 세정하는 단계를 더 포함하는 승화 정제 방법.And substituting a chemical solution of parts formed of metal in the first boat, the second boat, and the tube housing.
  18. 제16항에서,In claim 16,
    상기 세정하는 단계 이후에 베이킹하는 단계를 더 포함하는 승화 정제 방법.And a step of baking after the washing step.
  19. 제16항의 승화 정제 방법에 의해 정제된 유기 발광 소자용 물질.A material for an organic light-emitting device purified by the sublimation purification method of claim 16.
  20. 제19항의 유기 발광 소자용 물질을 포함하는 유기 발광 소자.An organic light-emitting device comprising the material for an organic light-emitting device of claim 19.
  21. 제1항에서,In claim 1,
    상기 챔버 내부에 고정되어 있는 승화 정제량 측정 부재를 더 포함하고,Further comprising a sublimation purification amount measuring member fixed in the chamber,
    상기 승화 정제량 측정 부재는 상기 보우트의 하부에 위치하는 승화 정제 장치.The sublimation purification amount measuring member is a sublimation purification device located at the bottom of the boat.
  22. 제8항에서,In claim 8,
    상기 챔버 내부에 고정되어 있는 승화 정제량 측정 부재를 더 포함하고,Further comprising a sublimation purification amount measuring member fixed in the chamber,
    상기 승화 정제량 측정 부재는 상기 보우트의 하부에 위치하는 승화 정제 장치.The sublimation purification amount measuring member is a sublimation purification device located at the bottom of the boat.
  23. 제22항에서,In claim 22,
    상기 제1 보우트와 상기 제2 보우트 중 적어도 하나는 상기 게이트를 통과한 보우트를 상기 챔버 내에서 이동시켜 상기 튜브 하우징과 밀착되도록 하는 상하 이송 장치를 더 포함하는 승화 정제 장치.At least one of the first boat and the second boat further comprises a vertical transfer device that moves the boat passing through the gate in the chamber to be in close contact with the tube housing.
  24. 제23항에서,In claim 23,
    상기 이송 장치에 의해 상기 보우트가 상기 튜브 하우징으로부터 이격되어 상기 승화 정제량 측정 부재에 도달하여 승화 정제량을 측정하는 승화 정제 장치.A sublimation purification device for measuring the amount of sublimation purification by reaching the sublimation purification amount measurement member by the boat spaced apart from the tube housing by the transfer device.
PCT/KR2019/009812 2018-09-12 2019-08-06 Sublimation purification apparatus and sublimation purification method WO2020054974A1 (en)

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