KR101665013B1 - Chemical vaporizer for manufacturing semi-sonductor - Google Patents

Chemical vaporizer for manufacturing semi-sonductor Download PDF

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Publication number
KR101665013B1
KR101665013B1 KR1020150049406A KR20150049406A KR101665013B1 KR 101665013 B1 KR101665013 B1 KR 101665013B1 KR 1020150049406 A KR1020150049406 A KR 1020150049406A KR 20150049406 A KR20150049406 A KR 20150049406A KR 101665013 B1 KR101665013 B1 KR 101665013B1
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chemical liquid
chemical
heat transfer
liquid
chamber
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KR1020150049406A
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Korean (ko)
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KR20160105710A (en
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봉경환
박수남
최재호
김순철
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포이스주식회사
(주)씨엔원
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    • H01L21/205
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/02Manufacture or treatment of semiconductor devices or of parts thereof

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Manufacturing & Machinery (AREA)
  • Computer Hardware Design (AREA)
  • Microelectronics & Electronic Packaging (AREA)
  • Power Engineering (AREA)
  • Chemical Vapour Deposition (AREA)

Abstract

The present invention relates to a chemical vaporizer for semiconductor manufacturing, and more particularly, to a chemical vaporizer for semiconductor manufacturing, more particularly, to a chemical vaporizer for manufacturing semiconductors, in which a liquid chemical liquid is injected downward from the inside of a gasification chamber and a chemical liquid is vaporized into a gas state by laminating heat transfer blades The present invention relates to a chemical vaporizer for semiconductor manufacturing, which maximizes vaporization efficiency by differentiating and controlling the temperature of a block heater provided outside the vaporization chamber in each vertical region.
According to the present invention, it is possible to easily change the chemical liquid in the liquid state to the gaseous state, and it is possible to maximize the vaporization efficiency by allowing heat transfer to occur in the chemical liquid well.

Description

{CHEMICAL VAPORIZER FOR MANUFACTURING SEMI-SONDUCTOR}

The present invention relates to a chemical vaporizer for semiconductor manufacturing, and more particularly, to a chemical vaporizer for semiconductor manufacturing, and more particularly, to a chemical vaporizer for chemical vapor deposition The present invention relates to a chemical vaporizer for semiconductor manufacturing, which maximizes vaporization efficiency by differentiating and controlling the temperature of a block heater provided outside the vaporization chamber in each vertical region.

Generally, in manufacturing processes related to semiconductors and electronic materials, an organometallic chemical or an inorganic metal chemical (hereinafter referred to as "chemical") is used when depositing a ceramic thin film and a thick film such as a metal thin film, a metal nitride thin film, A process such as Atomic Layer Deposition (ALD) or Chemical Vapor Deposition (CVD) is used.

Because of the low vapor pressure at room temperature, the bubbling vaporization technique has been developed to produce air bubbles by mixing a carrier gas such as simple nitrogen or argon into the above-mentioned chemicals. However, since such a technique alone makes it difficult to obtain a desired amount of vaporization sufficiently, a vaporization system for vaporizing the chemical liquid by heating with a heating device has been used.

1 is a partial perspective view showing the structure of a vaporization system according to the prior art.

Referring to FIG. 1, a prior art vaporization system includes a body portion 10 and a bottom portion 50 detachably coupled to the body portion 10.

The body portion 10 includes an inlet portion 17 through which the chemical is introduced and a first flow path 11 connected to the inlet portion 17 to provide a path for the chemical to flow, an outlet 19 through which the chemical flows out, , And a second flow path (15) connected to the outlet (19) to provide a chemical flow path.

When the bottom portion 50 and the body portion 10 are detachably connected, the first flow path 11 and the second flow path 15 are connected to each other so that the chemical flows.

The bottom portion 50 includes a first opening 59, a second opening 55 connected to the first opening 59 and a chemical flow communication, and a discharge portion 53. Here, the first opening 59 and the second opening 55 are communicated with each other, and the discharge portion 53 is also communicated with the first opening 59 and the second opening 55. The first flow path 11 and the second flow path 15 also communicate with each other.

Here, the second flow path 15 is heated for normal vaporization.

The bottom portion 50 includes a protrusion and a recess, and when the bottom portion 50 and the body portion 10 are detachably coupled, the protrusion may be configured to be inserted into the recess.

The chemical liquid in the liquid state flowing through the first flow path 11 is heated and vaporized by a heater (not shown) while moving to the second flow path 15. The gaseous state chemical is discharged through the outlet 19 and used for the production of semiconductor or electronic materials.

However, in the prior art, there is no apparatus for allowing chemical vaporization to occur in the flow paths 11 and 15, which causes a problem of low vaporization efficiency. When chemicals that are not completely vaporized are supplied to the semiconductor production line, it is necessary to increase the contact area so that complete vaporization can occur because the production equipment may fail or the production product may fail.

KR 10-2013-0046870 A KR 10-2009-0090479 A

According to an aspect of the present invention, there is provided a method of controlling a flow rate of a chemical liquid, the method comprising: providing a plurality of heat transfer vanes in a chemical liquid flow direction in a vaporization chamber where vaporization of a chemical liquid occurs; So that the vaporization efficiency can be maximized.

Another object of the present invention is to provide a chemical vaporizer for semiconductor manufacturing, which makes the path of the chemical solution longer by staggering the positions and shapes of the through holes formed in the heat transfer blades at the upper and lower ends.

A vaporizer for vaporizing and supplying a chemical solution used in a semiconductor manufacturing apparatus, comprising: a block heater (110) having a hollow portion (111) formed in the center thereof and a plurality of heating devices (112) arranged therein to generate heat; A vaporization chamber 120 inserted into the hollow portion 111 of the block heater 110 and having a chemical solution injection space 121 formed therein for vaporizing the chemical solution while moving; A chemical liquid injecting unit 130 connected to the upper portion of the gasification chamber 120 to inject a liquid chemical liquid into the gasification chamber 120; A gas discharging unit 140 connected to the lower portion of the gasification chamber 120 to supply a gaseous vaporized chemical liquid to the semiconductor manufacturing apparatus; A vacuum pump line 150 for blowing a high-pressure gas transfer gas to the lower end of the gasification chamber 120 so that vaporized chemical liquid is pushed to the gas discharge unit 140; And a heat transfer vane 160 installed in the chemical liquid injection space 121 for transferring the heat generated in the block heater 110 to the chemical liquid and changing a flow path of the chemical liquid.

The heat transfer blade (160) includes a central fixed post (161); And a plate-shaped vane (162) having a plurality of through holes (162a) through which the chemical liquid passes, the plate vane (162) being laminated on the fixed column (161) 162a are installed at positions staggered from the through holes 162a of the adjacent plate-like vanes 162. [0054]

The heat transfer blade (160) includes a central fixed post (161); A closing blade (163) having a diameter smaller than an inner diameter of the chemical liquid ejection space (121); And an opening blade (164) having a diameter equal to an inner diameter of the chemical liquid ejection space and having a through hole (164a) through which the chemical liquid passes, wherein the closing blade (163) and the opening blade (164) And are alternately stacked on the columns 161 in the vertical direction.

The heat transfer blade (160) includes a central fixed post (161); And a toothed wing 165 having an unevenness formed in the circumference thereof, and the toothed wings 165 are stacked on the fixing post 161 in a state of being vertically spaced apart from each other.

According to another embodiment of the present invention, there is provided a vaporizer for vaporizing and supplying a chemical solution used in a semiconductor manufacturing apparatus, wherein a hollow portion 111 is formed in the center, and a plurality of heating devices 112 are arranged inside to generate heat A block heater 110; A chemical solution injection space 121 is formed in the hollow part 111 of the block heater 110 and is vaporized while the chemical solution moves and an annular blocking plate 122 is protruded from the inner wall surface A vaporization chamber 120; A chemical liquid injecting unit 130 connected to the upper portion of the gasification chamber 120 to inject a liquid chemical liquid into the gasification chamber 120; A gas discharging unit 140 connected to the lower portion of the gasification chamber 120 to supply a gaseous vaporized chemical liquid to the semiconductor manufacturing apparatus; A vacuum pump line 150 for blowing a high-pressure gas transfer gas to the lower end of the gasification chamber 120 so that vaporized chemical liquid is pushed to the gas discharge unit 140; And a heat transfer vane 160 installed in the chemical liquid injection space 121 for transferring the heat generated in the block heater 110 to the chemical liquid and changing a flow path of the chemical liquid.

The heat transfer blade (160) includes a central fixed post (161); And a diameter of the shut-off vane 166 is smaller than an inner diameter of the vaporization chamber 120. The diameter of the cut-off vane 166 is smaller than the inner diameter of the vaporization chamber 120 And is larger than the central circular hole of the blocking plate 122.

The present invention further includes a pipe heater (170) installed inside the fixed column (161) to generate heat.

According to the present invention, it is possible to easily change the chemical liquid in a liquid state to a gaseous state, and heat transfer to the chemical liquid can be performed well, thereby maximizing the vaporization efficiency.

In addition, it has the effect of maximizing the degree of vaporization and the speed of the chemical liquid through the temperature control of the plurality of heat transfer blades and the flow path of the chemical liquid and the flow path of the chemical liquid.

1 is a partial perspective view showing the structure of a vaporization system according to the prior art;
2 is a perspective view showing the entire structure of a vaporizer according to an embodiment of the present invention.
3 is an exploded perspective view showing the internal structure of the vaporizer.
4 is a partial perspective view showing the internal structure of the block heater.
5 is a partial perspective view showing the internal structure of the gasification chamber;
6 is a perspective view showing a structure of a heat transfer blade;
7 is a cross-sectional view showing a laminated structure of the heat transfer blades of FIG. 6;
8 is a cross-sectional view showing a flow path of the chemical liquid in the vaporization chamber.
9 is a sectional view showing a laminated structure of a heat transfer blade according to another embodiment.
10 is a cross-sectional view showing a flow path of the chemical liquid in the vaporization chamber.
11 is a partial perspective view showing the internal structure of a gasification chamber according to another embodiment.
12 is a perspective view showing a structure of the heat transfer blade of FIG.
13 is a plan view showing a structure of the heat transfer blade of FIG.
14 is a cross-sectional view showing a flow path of the chemical liquid in the vaporization chamber of FIG.
15 is a partial perspective view showing the internal structure of the vaporization chamber according to yet another embodiment;
16 is a plan view showing the structure of the heat transfer blade of FIG. 15;
17 is a cross-sectional view showing a flow path of a chemical liquid in the vaporization chamber of FIG. 15;

Hereinafter, a "chemical vaporizer for semiconductor manufacturing" (hereinafter referred to as a " vaporizer ") according to an embodiment of the present invention will be described with reference to the drawings.

FIG. 2 is a perspective view showing the entire structure of a vaporizer according to an embodiment of the present invention, and FIG. 3 is an exploded perspective view showing an internal structure of a vaporizer.

The vaporizer 100 of the present invention has a cylindrical shape standing vertically as a whole, a heating means is provided on the outside, and a passage through which a liquid chemical liquid moves is formed inside.

As the heating means, a hollow cylindrical block heater 110 is used. In the space inside the block heater 110, a vaporization chamber 120 in which the chemical liquid is moved and vaporized is inserted. A liquid injecting portion 130 is formed above the vaporization chamber 120 to supply a liquid chemical liquid. A gas discharging portion 140 is formed below the vaporizing chamber 120 to discharge a vaporized liquid chemical.

A vacuum pump line 150 connected to a vacuum pump (not shown) generating a suction force for discharging the vaporized chemical liquid to the outside of the vaporization chamber 120 when the vaporized chemical liquid is not used, Respectively. The discharged chemical liquid is discharged into a gas scrubber.

The block heater 110 is described as having a cylindrical shape and a hollow having a circular cross section at the center, but the shape may be different.

The chamber-side gas discharge unit 140 and the vacuum pump line 150 for the ALD process are installed at positions facing each other at the lower end of the gasification chamber 120. In some cases, the gas discharge unit 140 and the vacuum pump line 150 may be installed in parallel positions.

4 is a partial perspective view showing the internal structure of the block heater.

The block heater 110 includes a thermoelectric element, a tungsten heater, a semiconductor heating device, and the like. The block heater 110 generates heat according to the supply of current. Various heating devices such as the electric heater can be used.

A plurality of heating devices 112 are vertically arranged in a cylindrical block heater 110 having a hollow portion 111 in the center. The number of the heating devices 112 may vary depending on the size and the capacity of the block heater 110. Preferably, a plurality of heating devices 112 are stacked on top of each other, and the temperature of the individual heating devices 112 may be controlled by varying the amount of current.

Generally, the temperature of the chemical liquid is relatively low at the initial stage of vaporization, and the temperature is further lowered because the pressure is lowered while passing through the chemical liquid injecting unit 130. Therefore, the portion close to the chemical solution input portion 130 (the upper side in the drawing of the present invention) is kept at a high temperature and the lower far portion is kept at a relatively low temperature. The temperature of the block heater 110 and the temperature difference of each section are optimized by varying the amount of chemicals, the injection speed, and the temperature.

FIG. 6 is a perspective view showing the structure of the heat transfer blade, FIG. 7 is a cross-sectional view showing a lamination structure of the heat transfer blades of FIG. 6, and FIG. 8 is a cross- And FIG.

The vaporization chamber 120 forms a space to be vaporized into a gaseous state by the heat generated in the block heater 110 while the liquid chemical liquid is injected into fine particles and moved.

The interior of the gasification chamber 120 forms a space in which the chemical liquid can move at a high speed, and is formed into a cylindrical shape standing perpendicular to the ground so that the chemical liquid can be injected, moved, and vaporized smoothly.

A chemical solution input unit 130 is connected to the upper portion of the gasification chamber 120. The chemical solution input unit 130 is connected to a chemical storage device used for semiconductor manufacturing. The chemical liquid supplied from the storage device flows into the interior of the gasification chamber 120 through the chemical liquid input portion 130.

The chemical liquid injecting section 130 has an inlet 131 to which a pipe extending from the chemical storage device is connected, a tubular liquid moving pipe 132 to which the chemical liquid moves, and an end portion exposed inside the gasification chamber 120, And an injection nozzle 133 for jetting at a high speed.

The liquid chemical liquid injected through the injection nozzle 133 has the lowest pressure at the initial stage of injection, and then the pressure is continuously increased. As the vaporization progresses, the pressure of the gas reaches a certain level and then passes through the gas discharging unit 140 to the semiconductor manufacturing equipment.

The temperature and the density of the chemical liquid are highest when they are discharged from the injection nozzle 133, then drop rapidly, and rise again while passing through the gasification chamber 120.

The temperature of the block heater 110 can be selected from the data table created based on the experimental data on the reference gas. The length of the gasification chamber 120, the size of the cross section, and the injection amount of the chemical liquid can be optimized through analysis of experimental data.

The chemical liquid, which has been changed into the gaseous state in the gasification chamber 120, flows out through the gas discharge unit 140. The inlet of the gas discharging unit 140 is connected to the gasification chamber 120 and is a passage through which the vaporized chemical liquid enters, and is supplied to the semiconductor manufacturing apparatus through the outlet 142.

A vacuum pump line 150 is installed on the opposite side of the gas discharge unit 140 from the gasification chamber 120. The vacuum pump line inlet 151 connected to the gasification chamber 120 in the vacuum pump line 150 is used when the gas vaporized inside the gasification chamber 120 is not used in the semiconductor ALD production apparatus, And the vacuum pump line outlet 152 is a place where the introduced chemical liquid flows out to the waste disposal facility.

The vaporized chemical liquid collected at the lower end of the gasification chamber 120 is pushed toward the gas discharge unit 140 according to the degree of vacuum in the chamber of the semiconductor ALD production apparatus.

Inside the gasification chamber 120, a heat transfer blade 160 for changing a flow path is installed to efficiently transfer heat to the chemical liquid.

Depending on the vaporization point, density and vaporization amount of the chemical liquid, the heat transfer blades 160 include a block-type or single-piece pipe heater 170 to compensate the heat of vaporization of the heat transfer blades 160.

As shown in FIGS. 5 and 6, the heat transfer blades 160 are made of a structure in which a plurality of plate-shaped blades 162 are installed on the fixed columns 161 at the central portion. The plate-shaped vane 162 is an approximately circular thin plate made of a heat-transferable metal material. The plate-shaped vane 162 transfers the heat generated from the block heater 110 to the chemical liquid, and at the same time, changes the chemical liquid flow path so that the chemical liquid stays in the vaporization chamber 120 for a long time.

By preventing the chemical liquid from moving in a straight line, heat is transferred to the chemical liquid evenly over a long period of time, so that vaporization can be performed more easily. And prevents the vaporized chemical liquid from moving downward and then liquefying again as the temperature is lowered. For this purpose, the plate of the plate-like vane 162 is arranged so as to stand in a direction perpendicular to the movement path of the chemical liquid.

The plate-shaped vane 162 is provided with a through hole 162a through which the chemical liquid can pass. The size and shape of the through hole 162a may vary depending on the type and the capacity of the vaporizer 100.

Preferably, a plurality of through holes 162a are formed in the plate-shaped vane 162, but the through holes 162a of the plate vanes 162 stacked vertically are located at positions where they are staggered from each other. 7 shows an example of the shape and arrangement of the through holes 162a so that the through holes 162a of the upper and lower plate-like vanes 162 do not come in the same position. For example, if the through holes 162a formed in one plate-shaped vane 162 are arranged in a row at 12 o'clock and 6 o'clock centered on the center of the plate, the number of the plate vanes 162 The through hole 162a is disposed at 3 o'clock and 9 o'clock. As the positions of the through holes 162a of the adjacent plate-like vanes 162 are shifted, the chemical liquid flowing downward in the vaporization chamber 120 can not linearly move and the path is broken (see FIG. 8). In the bending process, the residence time of the chemical solution becomes long and the number of times of contact with the plate-shaped vane 162 increases, so that more heat transfer occurs. Therefore, there is an advantage that the chemical liquid is sufficiently vaporized.

Since the fixing post 161 and the plate-shaped vane 162 are manufactured in a structure in which they can be assembled, it is possible to easily replace the plate vane 162 when the plate vane 162 needs to be different according to the type and amount of the chemical solution.

It is preferable that the pipe heater 170 is installed inside the fixed post 161.

8, the liquid chemical liquid injected into the vaporization chamber 120 through the injection nozzle 133 above the vaporization chamber 120 is directed downward along the chemical liquid injection space 121, The temperature is raised by the heat generated in the pipe heater 110 and the pipe heater 170. The heat generated in the block heater 110 and the pipe heater 170 is transmitted to the plate-shaped vane 162 having a high thermal conductivity, and the temperature of the chemical solution is further raised while contacting the plate-shaped vane 162. When the temperature of the chemical liquid reaches the vaporization point or more, the liquid phase changes to the gaseous state. The rate of the gaseous chemical liquid will become larger as the temperature goes down the vaporization chamber 120.

The chemical liquid in the liquid state or gaseous state is downwardly moved by the plate-shaped vane 162, and when the vaporization progresses further, it reaches the lower part of the vaporization chamber 120, it becomes 100% gas state. The gaseous fully vaporized chemical liquid is sucked by the vacuum degree of the production equipment chamber for the semiconductor ALD process and discharged through the gas outlet 142. The discharged gaseous chemical liquid is put into the semiconductor manufacturing process.

FIG. 9 is a cross-sectional view illustrating a stacked structure of heat transfer blades according to another embodiment, and FIG. 10 is a cross-sectional view illustrating a flow path of a chemical solution in the vaporization chamber.

In the above-described example, the flow path of the chemical liquid is changed by making the positions of the through holes 162a different only in the state that the diameters of the discs stacked on the upper and lower portions are the same. The structure of the block heater 110, the pipe heater 170, and the vaporization chamber 120 are the same, and the structure of the heat transfer vane 160 installed in the vaporization chamber 120 is modified do.

As shown in FIG. 9, in another embodiment, the diameter and the shape of the wings stacked on the upper and lower sides are differently configured. That is, the blades 163 having no holes are used as the uppermost blades, and the open blades 164 having the through holes 164a are used under the blades 163. The closing blades 163 are made smaller than the inside diameter of the chemical liquid injecting space 121 and the opening blades 164 are made smaller than the inside diameter of the chemical liquid injecting space 121 It is the same as the inner diameter.

A space is formed between the rim of the closing blade 163 and the inner wall of the chemical liquid ejection space 121 because the diameter of the closing blade 163 is smaller than the diameter of the chemical liquid ejection space 121 although there is no hole through which the chemical liquid can move. The chemical solution can move into this space.

A through hole 164a is formed in the opening blade 164. The shape or number of the through holes 164a may be different, but is formed so as to have a relatively large area near the center of the disk of the opening blades 164.

In order to smoothly move the chemical liquid and prevent the change in speed or pressure, the area of the through-hole 164a formed in the inside of the open vane 164 and the moving space formed in the rim of the closing vane 163 are made equal .

By stacking the closing blades 163 and the opening blades 164 alternately in this way, the movement path of the chemical liquid can be made to be curved as shown in FIG.

11 is a perspective view showing the internal structure of the vaporization chamber according to yet another embodiment, FIG. 12 is a perspective view showing the structure of the heat transfer blade shown in FIG. 11, FIG. 13 is a plan view showing the structure of the heat transfer blade shown in FIG. 14 is a cross-sectional view showing the flow path of the chemical liquid in the vaporization chamber of FIG.

The heat transfer blades 160 shown in FIGS. 11 to 14 are provided with fixing pillars 161 inside the vaporizing chamber 120 of the same type as the conventional ones and are stacked on the surface of the fixing pillars 161 at regular intervals Structure.

Unlike the previously used structure, the serrated blades 165 are used, and unevenness is formed in the circumference like a general sawtooth shape so as to be shaped like a toothed wheel. So that the chemical liquid flows out into the space between the teeth and the space between the walls of the gasification chamber 120.

The spaces between the teeth are shifted from each other in the serrated wings 165 stacked one above the other so that the chemical solution can flow in a curve instead of a straight line. As a result, the contact area between the chemical liquid and the serration vanes 165 becomes wider and the flow path becomes longer. Therefore, the heat transfer efficiency becomes higher.

15 is a partial perspective view showing the internal structure of the vaporization chamber according to yet another embodiment, FIG. 16 is a plan view showing the structure of the heat transfer blade of FIG. 15, and FIG. 17 is a cross- Fig.

In the three previous embodiments, no structure is formed on the inner wall of the vaporization chamber 120, so that the chemical solution can flow out without any resistance by removing the vanes provided inside.

In the fourth embodiment, a protruding structure is formed on the wall surface of the chemical liquid injection space 121 together with the wings.

As shown in FIG. 15, an annular blocking plate 122 cut in half is formed to protrude from the inner wall surface of the vaporization chamber 120. The blocking plate 122 is a relatively thin plate, which is formed to protrude at right angles from the wall surface. The blocking plates 122 are provided on the inner wall surface at a predetermined distance. A circular hole is formed in the center of the blocking plate 122 to serve as a passage for the chemical liquid.

A plurality of blocking blades 166 are provided on the surface of the center fixing post 161. It is most preferable that the blocking plate 122 and blocking blades 166 are in a state perpendicular to the moving direction of the chemical liquid.

The blocking blade 166 is a disk without any through-hole, and is provided on the surface of the fixed column 161 one by one at regular intervals. Preferably, the height is set so as to be located in the middle between the two blocking plates 122.

The diameter of the blocking blade 166 as a disk is smaller than the inner diameter of the gasification chamber 120 and larger than the central circular hole of the blocking plate 122. 16, since the circle of the blocking blade 166 is larger than the circle of the center hole of the blocking plate 122 when looking at the center of the upper portion of the vaporization chamber 120, the two are partially overlapped and the passage is obscured . In this state, as shown in FIG. 17, the chemical liquid turns around the outer periphery of the blocking blade 166 and turns toward the center direction. Then, the air passes through the hole in the blocking plate 122, and then returns to the outside of the circumference of the blocking blade 166.

Due to this structure, the chemical liquid moves downward along the course of the curve. In this process, the residence time is extended and the contact area is increased.

While the present invention has been described with reference to exemplary embodiments, it is to be understood that the invention is not limited to the disclosed embodiments, but, on the contrary, As will be understood by those skilled in the art. Therefore, it should be understood that the above-described embodiments are to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than the foregoing description, It is intended that all changes and modifications derived from the equivalent concept be included within the scope of the present invention.

100: carburetor 110: block heater
111: hollow part 112: heating device
120: gasification chamber 121: chemical liquid injection space
122: Blocking plate 130:
131: inlet 132: liquid flow tube
133: injection nozzle 140:
141: inlet 142: outlet
150: Vacuum pump line 151: Vacuum pump line inlet
152: vacuum pump line outlet 160: heat transfer blade
161: fixed post 162: plate-shaped blade
162a, 164a: through hole 163: closing blade
164: open wing 165: serrated wing
166: blocking blade 170: pipe heater

Claims (7)

delete delete delete delete A vaporizer for vaporizing and supplying a chemical solution used in a semiconductor manufacturing apparatus,
A hollow heater 111 is formed in the center, and a plurality of heating devices 112 are arranged vertically to generate heat;
A chemical solution injection space 121 is formed in the hollow part 111 of the block heater 110 and is vaporized while the chemical solution moves and an annular blocking plate 122 is protruded from the inner wall surface A vaporization chamber 120;
A chemical liquid injecting unit 130 connected to the upper portion of the gasification chamber 120 to inject liquid chemical liquid into the gasification chamber 120;
A gas discharging unit 140 connected to the lower portion of the gasification chamber 120 to supply a gaseous vaporized chemical liquid to the semiconductor manufacturing apparatus;
The gas supply unit 120 is installed at the lower side of the gasification chamber 120 on the opposite side of the gas discharge unit 140 with respect to the gasification chamber 120 and supplies the chemical solution vaporized in the gasification chamber 120 to the semiconductor manufacturing apparatus A vacuum pump line 150 for discharging the chemical solution remaining in the vaporization chamber 120 to a waste facility when the chemical solution is not present;
A heat transfer blade (160) installed in the chemical liquid injection space (121) and changing the flow path of the chemical liquid to increase the residence time;
And a pipe heater 170 for generating heat in the heat transfer blades 160 to heat the heat transfer blades 160,
The heat transfer blade (160)
A center pillar 161 in which a pipe heater 170 generating heat is installed;
And a blocking blade (166) provided on the surface of the fixing post (161) at a height at which the blocking plate (122) is not formed,
The blocking plate 122 has a circular through-hole at the center thereof,
Wherein the diameter of the blocking blade (166) is smaller than the inner diameter of the vaporization chamber (120) and larger than the central circular hole of the blocking plate (122).
delete delete
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KR20220105317A (en) 2021-01-20 2022-07-27 주식회사 메카로 Vaporizer for semiconductor process using carrier gas
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Publication number Priority date Publication date Assignee Title
JP2002359238A (en) * 2001-06-01 2002-12-13 Tokyo Electron Ltd Solid raw material vaporization apparatus and method

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KR100331024B1 (en) * 2000-06-05 2002-04-03 김상호 Liquid source injection vaporizer
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KR20090090479A (en) 2008-02-21 2009-08-26 (주)지오엘리먼트 Vaporization apparatus with high vaporiazation efficiency
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