WO2010122972A1 - Liquid raw material vaporizer - Google Patents

Liquid raw material vaporizer Download PDF

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Publication number
WO2010122972A1
WO2010122972A1 PCT/JP2010/056908 JP2010056908W WO2010122972A1 WO 2010122972 A1 WO2010122972 A1 WO 2010122972A1 JP 2010056908 W JP2010056908 W JP 2010056908W WO 2010122972 A1 WO2010122972 A1 WO 2010122972A1
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raw material
liquid raw
liquid
heater
container
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PCT/JP2010/056908
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French (fr)
Japanese (ja)
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孝之 家城
達也 林
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株式会社堀場エステック
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Application filed by 株式会社堀場エステック filed Critical 株式会社堀場エステック
Priority to CN2010800137038A priority Critical patent/CN102365388A/en
Priority to US13/265,845 priority patent/US20120042838A1/en
Priority to JP2010515300A priority patent/JP5702139B2/en
Publication of WO2010122972A1 publication Critical patent/WO2010122972A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01BBOILING; BOILING APPARATUS ; EVAPORATION; EVAPORATION APPARATUS
    • B01B1/00Boiling; Boiling apparatus for physical or chemical purposes ; Evaporation in general
    • B01B1/02Preventing foaming
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/14Evaporating with heated gases or vapours or liquids in contact with the liquid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/30Accessories for evaporators ; Constructional details thereof

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  • the present invention relates to a liquid raw material vaporizer that vaporizes a liquid raw material by a bubbling method using a carrier gas.
  • a liquid source container for storing a liquid source and a carrier gas for bubbling the liquid source stored in the liquid source container with a carrier gas Some have an introduction pipe and a bubbling gas output pipe connected to the upper space (gas phase) of the liquid source container and for supplying the bubbling gas outside the liquid source container. And the front-end
  • the liquid raw material is vaporized in the bubbles, so that the gasified raw material is supplied to the outside together with the carrier gas.
  • a heater for heating the stored liquid material to a constant temperature is provided on the outer surface of the liquid material container, and the liquid material is configured to have a uniform temperature distribution.
  • the liquid source container is large, the bubble moving region generated by the bubbling nozzle is limited to a part, so the stirring effect of the liquid source due to the bubbles cannot be obtained, and the temperature distribution of the liquid source is reduced. There is a problem that it is difficult to keep it uniform. If the liquid source container is enlarged, it is difficult to heat the liquid source so that the temperature distribution of the liquid source is uniform only by providing a heater on the outer surface of the liquid source container.
  • a bubbling nozzle may be provided so that the bubbles hit the inner surface of the liquid source container, and the liquid source may be stirred.
  • the bubbles adhere to the inner surface of the liquid source, and the bubbles recombine with each other. The problem will be that the bubbles will become enlarged.
  • the present invention has been made to solve the above problems all at once, and prevents recombination of bubbles to suppress the enlargement of bubbles and make the temperature distribution of the stored liquid raw material uniform. This is the main desired issue.
  • the liquid raw material vaporizer includes a liquid raw material container in which the liquid raw material is stored, a first heater that is provided on at least the side wall of the liquid raw material container and heats the stored liquid raw material, A second heater provided inside the liquid source container for heating the stored liquid source, and immersed in the stored liquid source, and between the second heater and the side wall And a plurality of bubble generators for discharging and bubbling a carrier gas into the liquid raw material, and a gas supply pipe for supplying the carrier gas to the bubble generator.
  • the 1st heater and the 2nd heater are provided in the side wall and internal central part of a liquid source container, temperature distribution of the liquid source stored in the liquid source container is made uniform. Can be easily. Further, since the bubble generator is provided between the second heater and the inner surface of the side wall, it is possible to make it difficult for the air bubbles to come into contact with the second heater and the inner surface of the side wall. Can be prevented. Further, convection can be formed in the liquid source container, and the liquid source can be stirred. Furthermore, by providing a plurality of bubble generators, even if the liquid source container is large, the agitation effect of the liquid source can be sufficiently exerted by the bubbles generated by each bubble generator and stored. The temperature distribution of the liquid raw material can be made uniform easily.
  • the temperature distribution of the liquid source can be made more uniform by the bubbles generated by the bubble generator.
  • the vicinity of the second heater is in the temperature gradient region generated between the second heater and the liquid raw material, and in the state where bubbles are generated, the influence of the bubbles attached to the second heater. Is a position that can be substantially ignored.
  • the plurality of bubble generators be provided radially and equidistantly about the central axis of the liquid material container.
  • the plurality of bubble generators In order to make the temperature distribution of the liquid material uniform with high accuracy by making the bubbles generated from each bubble generator constant, the plurality of bubble generators have the same configuration, and the gas supply pipes are It is desirable to provide a constant flow device for supplying a carrier gas having a constant flow rate to the plurality of bubble generators.
  • the recombination of bubbles can be prevented to suppress the enlargement of bubbles, and the temperature of the liquid material stored in the liquid material container can be made uniform.
  • FIG. 1 is an overall configuration diagram of a liquid raw material vaporizer according to an embodiment of the present invention. It is a schematic diagram which shows the arrangement
  • the liquid source vaporization apparatus 100 is a device that vaporizes and supplies a liquid source serving as a film forming source to a film forming apparatus using a CVD method or the like by a bubbling method, as shown in FIG.
  • a liquid raw material container 2 in which a liquid raw material such as tetraethoxysilane (TEOS) is stored, and provided on the side wall, upper wall, and lower wall of the liquid raw material container 2 for heating the stored liquid raw material to a predetermined temperature.
  • TEOS tetraethoxysilane
  • a plurality of bubble generators 5 provided between the second heater 4 and the side wall for discharging and bubbling a carrier gas into the liquid raw material, and a carrier such as nitrogen or argon in the bubble generator 5 Gas supply Comprising a gas supply pipe 6, the.
  • the liquid raw material container 2 is a stainless steel sealed container having a substantially rotating body shape.
  • an upper space (gas phase) formed in a state where the liquid raw material is stored the vaporized liquid raw material after bubbling is used as a carrier gas.
  • a gas outlet pipe 7 for supplying to a film forming apparatus (not shown) is connected.
  • the figure in which the gas outlet pipe 7 is connected to the upper wall of the liquid raw material container 2 in FIG. 1 is shown.
  • the first heater 3 is provided in contact with or close to the entire outer surface of the side wall, upper wall, and lower wall of the liquid source container 2. Further, the second heater 4 is supported and provided on the upper wall so as to extend in the vertical direction at the inner central portion of the liquid source container 2. Note that the first heater 3 and the second heater 4 are heated to the same temperature (for example, 50 ° C.) by a control unit (not shown) in order to heat the liquid raw material to a predetermined temperature (for example, 50 ° C.). .
  • the bubble generator 5 discharges a carrier gas into the liquid raw material to form a large number of bubbles having a predetermined diameter, and the configuration of each bubble generator 5 is the same.
  • the diameter of the bubble is such that the liquid source vaporizes and saturates in the bubble, and is about 1 mm, for example.
  • the flow rate of the carrier gas supplied to the bubble generator 5 is determined by a mass flow controller (MFC) 8 and a constant flow device, which will be described later.
  • MFC mass flow controller
  • the bubble generator 5 is provided in the vicinity of the bottom of the liquid raw material container 2. Specifically, the bubble generator 5 is positioned below the second heater 4 and radially outside the second heater 4. Is provided. More specifically, the bubble generator 5 is provided so that bubbles generated by the bubble generator 5 pass through the vicinity of the inner surface of the side wall of the liquid source container 2 and the vicinity of the second heater 4. In the present embodiment, the bubble generator 5 extends from the vicinity of the second heater 4 to the vicinity of the side wall of the container 2 between the second heater 4 and the side wall of the container 2 as shown in FIG. Is provided. That is, in the vertical projection, the second heater 4 and the side wall of the container 2 and the bubble generator 5 are provided so as not to overlap each other. Further, as shown in FIG. 2, the bubble generators 5 are provided radially and equidistantly about the central axis C of the liquid raw material container 2.
  • the vicinity of the second heater 4 is a temperature gradient region generated between the second heater 4 and the liquid material (“temperature gradient region on the second heater side” in FIG. 3). ) And in a state where bubbles are generated, the position is such that the influence of the bubbles attached to the second heater 4 can be substantially ignored.
  • the vicinity of the inner surface of the side wall refers to the inner surface of the side wall in the temperature gradient region (the “temperature gradient region on the side wall side” in FIG. 3) generated between the inner surface of the side wall and the liquid raw material. This is a position where the effect of vaporization efficiency due to the adhesion of bubbles to the surface can be substantially ignored.
  • the temperature gradient region is a region where the temperature of the liquid material changes as the liquid material moves away from the heaters 3 and 4 in the horizontal direction at the liquid surface or a predetermined depth.
  • FIG. 3 shows the temperature distribution of the liquid source at a predetermined depth X and its temperature gradient region.
  • the temperature gradient region generated between the second heater 4 and the liquid raw material is different when the operation of the second heater 4 starts (at the start of heating) and when the heating is stable, and is heated more than the temperature gradient region at the start of the operation.
  • the stable temperature gradient region is narrower. Therefore, in order to bring the bubble generator 5 as close as possible to the second heater 4, it is preferable that the bubble generator 5 is provided in a temperature gradient region generated between the inner surface of the side wall and the liquid raw material at the time of stable heating.
  • the temperature gradient region generated between the inner surface of the side wall and the liquid raw material is different at the start of operation of the first heater 3 (at the start of heating) and at the time of stable heating, and more stable than the temperature gradient region at the start of operation.
  • the temperature gradient region at the time is narrower. Therefore, in order to bring the bubble generator 5 as close as possible to the inner surface of the side wall, it is preferable that the bubble generator 5 is provided in a temperature gradient region generated between the inner surface of the side wall and the liquid material at the time of stable heating.
  • the gas supply pipe 6 is provided by being inserted into the liquid source container 2 from the upper wall, and is provided along the second heater 4 in this embodiment. Specifically, the gas supply pipe 6 is provided by being inserted from the upper wall of the liquid source container 2 into the inside, and extends along the second heater 4 to the lower end of the lower end thereof, and the lower end of the main pipe 61. And a plurality of branch pipes 62 extending in the radial direction of the liquid raw material container 2.
  • the main pipe 61 is provided so that its pipe axis is substantially parallel to the central axis C of the liquid source container 2, and the branch pipe 62 is radially and radially in a direction substantially perpendicular to the pipe axis of the main pipe 61. Are branched at equal intervals.
  • the bubble generator 5 is connected to the tip of the branch pipe 62. That is, the gas supply pipe 6 is configured to be branched on the lower side below the lower end of the second heater 4.
  • the main pipe 61 is provided with a mass flow controller (MFC) 8 for controlling the flow rate of the carrier gas and a preheater 9 for preheating the carrier gas.
  • MFC mass flow controller
  • the pipe of only the main pipe 61 exists in the upper part of the bubble generator 5, so that the pipe structure of the upper part of the bubble generator 5 can be simplified, and the bubbles generated from the bubble generator 5 come into contact with the pipe. Can be suppressed as much as possible.
  • the branch pipe 62 and the bubble generator 5 are connected by a pipe joint 10 such as a VCR joint, for example.
  • the orifice as a constant flow device is comprised by making small the opening diameter of the cyclic
  • FIG. The pipe joints 10 of the respective branch passages 62 and the respective bubble generators 5 have the same configuration, and the sealing material 11 therein also has the same configuration. Thereby, it is comprised so that the supply flow rate of the carrier gas supplied to each bubble generator 5 may become the same.
  • the carrier gas supply pipe is composed of one main pipe and a plurality of branch pipes, but one carrier gas supply pipe is provided for each bubble generator without branching the carrier gas supply pipe. May be provided. Further, a plurality of bubble generators may be grouped, and a carrier gas supply pipe similar to that of the above embodiment may be provided for each group.
  • connection position of the carrier gas supply pipe is not limited to the upper wall of the liquid source container, and may be a side wall or a lower wall.
  • the constant flow device provided in the branch pipe of a carrier gas supply pipe is comprised using the sealing material provided in a VCR joint inside, it is made to provide a constant flow device separately on a branch pipe. Also good.
  • FIG. 5 by supplying a plurality of bubble generators as a group, carrier gas supply pipes 6A and 6B are provided for each group, and switching valves V are provided in the supply pipes 6A and 6B. You may comprise so that the liquid raw material may be vaporized by switching the pipes 6A and 6B.
  • a pressure sensor P for measuring the pressure in each of the supply pipes 6A and 6B is provided, and the bubble generator 5 is clogged when the pressure in one of the supply pipes used is increased to a predetermined value or more. Therefore, bubbles are generated by switching to the other supply pipe.
  • FIG. 5 by supplying a plurality of bubble generators as a group, carrier gas supply pipes 6A and 6B are provided for each group, and switching valves V are provided in the supply pipes 6A and 6B. You may comprise so that the liquid raw material may be vaporized by switching the pipes 6A and 6B.
  • a pressure sensor P for measuring the pressure in each of the supply pipes 6A and 6B is provided, and the bubble generator 5 is c
  • FIG 5 shows a configuration in which the carrier gas supply pipes 6A and 6B merge on the upstream side and a pressure sensor P is provided at the junction to measure the pressure.
  • a pressure sensor P is provided at the junction to measure the pressure.
  • the liquid material vaporization apparatus of the above embodiment is configured using a plurality of bubble generators.
  • a single bubble generator having an annular shape (for example, an annular shape) is used to surround the second heater. It may be configured.
  • the four bubble generators are provided.
  • the number of bubble generators can be appropriately changed depending on the configuration of the flow rate of the carrier gas or the size and shape of the liquid source container.
  • the bubble generators are provided radially at equal intervals, but the arrangement mode of the bubble generators can be changed as appropriate depending on the configuration in the liquid source container.
  • the liquid raw material vaporizer of the embodiment does not have the second heater, the liquid raw material can be vaporized, but if the liquid raw material container is enlarged, the vaporization efficiency is lowered. On the other hand, if the liquid material container is small, the liquid material can be sufficiently vaporized only by the first heater.
  • the liquid source vaporizer is provided on at least the side wall of the liquid source container in which the liquid source is stored and the liquid source container, and heats the stored liquid source And a plurality of bubble generators for immersing in the stored liquid raw material, releasing a carrier gas into the liquid raw material and bubbling, and supplying the carrier gas to the bubble generator It is desirable that a plurality of bubble generators be provided so that bubbles generated by the plurality of bubble generators pass in the vicinity of the inner surface of the side wall of the liquid raw material container.
  • the recombination of bubbles can be prevented to suppress the enlargement of bubbles, and the temperature of the liquid raw material stored in the liquid raw material container can be made uniform.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Chemical Vapour Deposition (AREA)

Abstract

A liquid raw material vaporizer which minimizes the bloating of bubbles by preventing recombination of bubbles and equalizes the temperature distribution of stored liquid raw material comprises a liquid raw material container (2), a first heater (3) mounted on the sidewall of the liquid raw material container (2) in order to heat the stored liquid raw material to a predetermined temperature, a second heater (4) provided at the central part in the liquid raw material container (2) in order to heat the stored liquid raw material to a predetermined temperature, a plurality of bubble generators (5) provided between the second heater (4) and the sidewall while being immersed in the stored liquid raw material in order to bubble the liquid raw material by discharging carrier gas into the liquid raw material, and a gas supply pipe (6) which supplies carrier gas to the bubble generators (5).

Description

液体原料気化装置Liquid raw material vaporizer
 本発明は、キャリアガスを用いたバブリング法により液体原料を気化させる液体原料気化装置に関するものである。 The present invention relates to a liquid raw material vaporizer that vaporizes a liquid raw material by a bubbling method using a carrier gas.
 この種の液体原料気化装置としては、例えば特許文献1に示すように、液体原料を貯留する液体原料容器と、当該液体原料容器内に貯留された液体原料をキャリアガスによってバブリングするためのキャリアガス導入管と、液体原料容器の上部空間(気相)に接続され、バブリング後のガスを液体原料容器外に供給するためのバブリングガス出力管とを備えるものがある。そして、キャリアガス導入管の先端部は液体原料に浸漬され、その先端部には、複数の細管で構成されるバブリングノズルが接続されている。このバブリングノズルにより生じた気泡が液体原料中を浮き上がっていく過程で、気泡中に液体原料を気化させることによって、キャリアガスとともに気体になった原料が外部に供給される。また、液体原料容器の外面には、貯留する液体原料を一定温度に加熱するためのヒータが設けられ、液体原料を均一な温度分布にすべく構成されている。 As this type of liquid source vaporizer, for example, as shown in Patent Document 1, a liquid source container for storing a liquid source and a carrier gas for bubbling the liquid source stored in the liquid source container with a carrier gas Some have an introduction pipe and a bubbling gas output pipe connected to the upper space (gas phase) of the liquid source container and for supplying the bubbling gas outside the liquid source container. And the front-end | tip part of a carrier gas introduction pipe | tube is immersed in the liquid raw material, The bubbling nozzle comprised by a some thin tube is connected to the front-end | tip part. In the process in which bubbles generated by the bubbling nozzle float up in the liquid raw material, the liquid raw material is vaporized in the bubbles, so that the gasified raw material is supplied to the outside together with the carrier gas. Further, a heater for heating the stored liquid material to a constant temperature is provided on the outer surface of the liquid material container, and the liquid material is configured to have a uniform temperature distribution.
 しかしながら、バブリングノズルにより生じた気泡は、液体原料容器内面又はその容器内の構成部品に付着してしまい、これによって気泡同士が再結合し、気泡が肥大化してしまうという問題がある。このように気泡が肥大化してしまうと、液体原料が気泡中に気化する割合が小さくなってしまい、気泡中に液体原料を飽和させることができず、気化効率が低下してしまう。 However, there is a problem that bubbles generated by the bubbling nozzle adhere to the inner surface of the liquid raw material container or the components in the container, thereby recombining the bubbles and enlarging the bubbles. When the bubbles are enlarged as described above, the rate at which the liquid raw material is vaporized in the bubbles becomes small, the liquid raw material cannot be saturated in the bubbles, and the vaporization efficiency is lowered.
 また、液体原料容器が大型のものであれば、バブリングノズルによって生じた気泡の移動領域が一部に限定されてしまうため、気泡による液体原料の攪拌効果が得られず、液体原料の温度分布を均一に保つことが難しくなるという問題がある。なお、液体原料容器が大型化すれば、ヒータを液体原料容器の外面に設けるだけでは、液体原料の温度分布を均一にするように加熱することが難しくなるという問題もある。ここで、バブリングノズルを気泡が液体原料容器の内面に当たるように設け、液体原料を攪拌させることも考えられるが、上述したように液体原料内面に気泡が付着し、これによって気泡同士が再結合し、気泡が肥大化してしまうという問題が生じてしまう。 In addition, if the liquid source container is large, the bubble moving region generated by the bubbling nozzle is limited to a part, so the stirring effect of the liquid source due to the bubbles cannot be obtained, and the temperature distribution of the liquid source is reduced. There is a problem that it is difficult to keep it uniform. If the liquid source container is enlarged, it is difficult to heat the liquid source so that the temperature distribution of the liquid source is uniform only by providing a heater on the outer surface of the liquid source container. Here, a bubbling nozzle may be provided so that the bubbles hit the inner surface of the liquid source container, and the liquid source may be stirred. However, as described above, the bubbles adhere to the inner surface of the liquid source, and the bubbles recombine with each other. The problem will be that the bubbles will become enlarged.
特開平06-267852号公報Japanese Patent Application Laid-Open No. 06-267852
 そこで本発明は、上記問題点を一挙に解決するためになされたものであり、気泡の再結合を防止して気泡の肥大化を抑制するとともに、貯留された液体原料の温度分布を均一にすることをその主たる所期課題とするものである。 Therefore, the present invention has been made to solve the above problems all at once, and prevents recombination of bubbles to suppress the enlargement of bubbles and make the temperature distribution of the stored liquid raw material uniform. This is the main desired issue.
 すなわち本発明に係る液体原料気化装置は、液体原料が貯留される液体原料容器と、前記液体原料容器の少なくとも側壁に設けられて、貯留された液体原料を加熱するための第1のヒータと、前記液体原料容器の内部に設けられて、貯留された液体原料を加熱するための第2のヒータと、貯留された液体原料中に浸漬されるとともに、前記第2のヒータ及び側壁との間に設けられ、前記液体原料中にキャリアガスを放出してバブリングするための複数の気泡発生器と、前記気泡発生器にキャリアガスを供給するガス供給管と、を備えることを特徴とする。 That is, the liquid raw material vaporizer according to the present invention includes a liquid raw material container in which the liquid raw material is stored, a first heater that is provided on at least the side wall of the liquid raw material container and heats the stored liquid raw material, A second heater provided inside the liquid source container for heating the stored liquid source, and immersed in the stored liquid source, and between the second heater and the side wall And a plurality of bubble generators for discharging and bubbling a carrier gas into the liquid raw material, and a gas supply pipe for supplying the carrier gas to the bubble generator.
 このようなものであれば、液体原料容器の側壁及び内部中央部に第1のヒータ及び第2のヒータを設けているので、液体原料容器内に貯留された液体原料の温度分布の均一化を容易にすることができる。また、気泡発生器を第2のヒータ及び側壁内面の間に設けているので、第2のヒータ及び側壁内面に気泡を接触しにくくすることができ、それらに気泡が付着することによる気泡の肥大化を防ぐことができる。また、液体原料容器内に対流を形成することもでき、液体原料の攪拌を行うことができる。さらに、複数の気泡発生器を設けることによって、液体原料容器が大型のものであっても、各気泡発生器により生じた気泡により液体原料の攪拌効果を十分に発揮することができ、貯留された液体原料の温度分布の均一化を容易にすることができる。 If it is such, since the 1st heater and the 2nd heater are provided in the side wall and internal central part of a liquid source container, temperature distribution of the liquid source stored in the liquid source container is made uniform. Can be easily. Further, since the bubble generator is provided between the second heater and the inner surface of the side wall, it is possible to make it difficult for the air bubbles to come into contact with the second heater and the inner surface of the side wall. Can be prevented. Further, convection can be formed in the liquid source container, and the liquid source can be stirred. Furthermore, by providing a plurality of bubble generators, even if the liquid source container is large, the agitation effect of the liquid source can be sufficiently exerted by the bubbles generated by each bubble generator and stored. The temperature distribution of the liquid raw material can be made uniform easily.
 前記複数の気泡発生器により生じる気泡が、前記液体原料容器の側壁内面の近傍及び前記第2のヒータの近傍を通過するように、前記複数の気泡発生器が設けられていることによって、気泡を液体原料容器の側壁内面及び第2のヒータに付着しにくくしながらも、気泡発生器により生じた気泡により液体原料の温度分布を一層均一化させることができる。第2のヒータの近傍とは、第2のヒータと液体原料との間に生じる温度勾配領域内であって、且つ、気泡が生じている状態において、第2のヒータへの気泡の付着による影響が実質的に無視できる程度の位置である。側壁内面の近傍とは、側壁内面と液体原料との間に生じる温度勾配領域内であって、且つ、気泡が生じている状態において、側壁内面への気泡の付着による気化効率などの影響が実質的に無視できる程度の位置である。 By providing the plurality of bubble generators so that the bubbles generated by the plurality of bubble generators pass through the vicinity of the inner surface of the side wall of the liquid source container and the vicinity of the second heater, While being difficult to adhere to the inner surface of the side wall of the liquid source container and the second heater, the temperature distribution of the liquid source can be made more uniform by the bubbles generated by the bubble generator. The vicinity of the second heater is in the temperature gradient region generated between the second heater and the liquid raw material, and in the state where bubbles are generated, the influence of the bubbles attached to the second heater. Is a position that can be substantially ignored. In the vicinity of the inner surface of the side wall, in the temperature gradient region generated between the inner surface of the side wall and the liquid raw material, and in the state where bubbles are generated, the effect such as vaporization efficiency due to the adhesion of the bubbles to the inner surface of the side wall is substantial. The position is negligible.
 また、液体原料の温度分布をより一層均一化させるためには、前記複数の気泡発生器が前記液体原料容器の中心軸を中心として放射状に且つ等間隔に設けられていることが望ましい。 Also, in order to make the temperature distribution of the liquid material even more uniform, it is desirable that the plurality of bubble generators be provided radially and equidistantly about the central axis of the liquid material container.
 各気泡発生器から生じる気泡を一定にすることによって、液体原料の温度分布を精度良く均一にするためには、前記複数の気泡発生器が同一の構成のものであり、前記ガス供給管が、前記複数の気泡発生器に一定流量のキャリアガスを供給するための定流量器を備えることが望ましい。 In order to make the temperature distribution of the liquid material uniform with high accuracy by making the bubbles generated from each bubble generator constant, the plurality of bubble generators have the same configuration, and the gas supply pipes are It is desirable to provide a constant flow device for supplying a carrier gas having a constant flow rate to the plurality of bubble generators.
 このように構成した本発明によれば、気泡の再結合を防止して気泡の肥大化を抑制するとともに、液体原料容器に貯留された液体原料の温度を均一にすることができる。 According to the present invention configured as described above, the recombination of bubbles can be prevented to suppress the enlargement of bubbles, and the temperature of the liquid material stored in the liquid material container can be made uniform.
本発明の一実施形態に係る液体原料気化装置の全体構成図である。1 is an overall configuration diagram of a liquid raw material vaporizer according to an embodiment of the present invention. 同実施形態の気泡発生器の配置態様を示す模式図である。It is a schematic diagram which shows the arrangement | positioning aspect of the bubble generator of the embodiment. 側壁内面及び第2ヒータの間の液体原料の温度分布を示す図である。It is a figure which shows the temperature distribution of the liquid raw material between a side wall inner surface and a 2nd heater. 同実施形態の分岐管及び気泡発生器の管継手を示す断面図である。It is sectional drawing which shows the pipe joint of the branch pipe and bubble generator of the embodiment. 変形実施形態に係る液体原料気化装置を模式的に示す図である。It is a figure which shows typically the liquid raw material vaporization apparatus which concerns on deformation | transformation embodiment.
100・・・液体原料気化装置
2  ・・・液体原料容器
3  ・・・第1のヒータ
4  ・・・第2のヒータ
5  ・・・気泡発生器
6  ・・・ガス供給管
DESCRIPTION OF SYMBOLS 100 ... Liquid raw material vaporizer 2 ... Liquid raw material container 3 ... 1st heater 4 ... 2nd heater 5 ... Bubble generator 6 ... Gas supply pipe | tube
 以下に本発明に係る液体原料気化装置の一実施形態について図面を参照して説明する。 Hereinafter, an embodiment of a liquid raw material vaporizer according to the present invention will be described with reference to the drawings.
 本実施形態に係る液体原料気化装置100は、CVD法などを用いた成膜装置にその成膜原料となる液体原料をバブリング法により気化して供給するものであり、図1に示すように、テトラエトキシシラン(TEOS)等の液体原料が貯留される液体原料容器2と、液体原料容器2の側壁、上壁、下壁に設けられて、貯留された液体原料を所定温度に加熱するための第1のヒータ3と、液体原料容器2の内部中央部に設けられて、貯留された液体原料を所定温度に加熱するための第2のヒータ4と、貯留された液体原料中に浸漬されるとともに、第2のヒータ4及び側壁との間に設けられ、前記液体原料中にキャリアガスを放出してバブリングするための複数の気泡発生器5と、気泡発生器5に窒素又はアルゴン等のキャリアガスを供給するガス供給管6と、を備える。 The liquid source vaporization apparatus 100 according to the present embodiment is a device that vaporizes and supplies a liquid source serving as a film forming source to a film forming apparatus using a CVD method or the like by a bubbling method, as shown in FIG. A liquid raw material container 2 in which a liquid raw material such as tetraethoxysilane (TEOS) is stored, and provided on the side wall, upper wall, and lower wall of the liquid raw material container 2 for heating the stored liquid raw material to a predetermined temperature. A first heater 3, a second heater 4 provided at the center of the liquid source container 2 for heating the stored liquid source to a predetermined temperature, and immersed in the stored liquid source In addition, a plurality of bubble generators 5 provided between the second heater 4 and the side wall for discharging and bubbling a carrier gas into the liquid raw material, and a carrier such as nitrogen or argon in the bubble generator 5 Gas supply Comprising a gas supply pipe 6, the.
 液体原料容器2は、概略回転体形状をなすステンレス製の密閉容器であり、液体原料が貯留された状態において形成される上部空間(気相)には、バブリング後の気化した液体原料をキャリアガスとともに成膜装置(不図示)に供給するためのガス導出管7が接続されている。なお、図1においてガス導出管7が液体原料容器2の上壁に接続されている図を示している。 The liquid raw material container 2 is a stainless steel sealed container having a substantially rotating body shape. In an upper space (gas phase) formed in a state where the liquid raw material is stored, the vaporized liquid raw material after bubbling is used as a carrier gas. In addition, a gas outlet pipe 7 for supplying to a film forming apparatus (not shown) is connected. In addition, the figure in which the gas outlet pipe 7 is connected to the upper wall of the liquid raw material container 2 in FIG. 1 is shown.
 第1のヒータ3は、液体原料容器2の側壁、上壁及び下壁の外表面全体に接触又は近接して設けられている。また、第2のヒータ4は、液体原料容器2の内部中央部に上下方向に延びるように、上壁に支持されて設けられている。なお、第1のヒータ3及び第2のヒータ4は、液体原料を所定温度(例えば50℃)に加熱するために、図示しない制御部により同一の温度(例えば50℃)に昇温されている。 The first heater 3 is provided in contact with or close to the entire outer surface of the side wall, upper wall, and lower wall of the liquid source container 2. Further, the second heater 4 is supported and provided on the upper wall so as to extend in the vertical direction at the inner central portion of the liquid source container 2. Note that the first heater 3 and the second heater 4 are heated to the same temperature (for example, 50 ° C.) by a control unit (not shown) in order to heat the liquid raw material to a predetermined temperature (for example, 50 ° C.). .
 気泡発生器5は、液体原料中にキャリアガスを放出して所定径を有する多数の気泡を形成させるものであり、各気泡発生器5の構成は同一である。気泡の径は、浮上距離及び気泡中に液体原料が気化して飽和する程度のものであり、例えば1mm程度である。また、気泡発生器5に供給されるキャリアガスの流量は、後述するマスフローコントローラ(MFC)8及び定流量器により決定される。 The bubble generator 5 discharges a carrier gas into the liquid raw material to form a large number of bubbles having a predetermined diameter, and the configuration of each bubble generator 5 is the same. The diameter of the bubble is such that the liquid source vaporizes and saturates in the bubble, and is about 1 mm, for example. Further, the flow rate of the carrier gas supplied to the bubble generator 5 is determined by a mass flow controller (MFC) 8 and a constant flow device, which will be described later.
 また、気泡発生器5は、液体原料容器2の底部近傍に設けられており、具体的には、第2のヒータ4の下側において、第2のヒータ4の径方向外側に位置するように設けられている。より詳細には、気泡発生器5により生じる気泡が、液体原料容器2の側壁内面の近傍及び第2のヒータ4の近傍を通過するように、気泡発生器5が設けられている。本実施形態では、気泡発生器5は、図2に示すように、第2のヒータ4及び容器2の側壁との間において、第2のヒータ4の近傍から容器2の側壁の近傍に亘って設けられている。つまり、鉛直投影において、第2のヒータ4及び容器2側壁と気泡発生器5とが互いに重ならないように設けられている。さらに、気泡発生器5は、図2に示すように、液体原料容器2の中心軸Cを中心として放射状に且つ等間隔に設けられている。 The bubble generator 5 is provided in the vicinity of the bottom of the liquid raw material container 2. Specifically, the bubble generator 5 is positioned below the second heater 4 and radially outside the second heater 4. Is provided. More specifically, the bubble generator 5 is provided so that bubbles generated by the bubble generator 5 pass through the vicinity of the inner surface of the side wall of the liquid source container 2 and the vicinity of the second heater 4. In the present embodiment, the bubble generator 5 extends from the vicinity of the second heater 4 to the vicinity of the side wall of the container 2 between the second heater 4 and the side wall of the container 2 as shown in FIG. Is provided. That is, in the vertical projection, the second heater 4 and the side wall of the container 2 and the bubble generator 5 are provided so as not to overlap each other. Further, as shown in FIG. 2, the bubble generators 5 are provided radially and equidistantly about the central axis C of the liquid raw material container 2.
 ここで、第2のヒータ4の近傍とは、図3に示すように、第2のヒータ4と液体原料との間に生じる温度勾配領域(図3の「第2ヒータ側の温度勾配領域」)内であって、且つ、気泡が生じている状態において、第2のヒータ4への気泡の付着による影響が実質的に無視できる程度の位置である。側壁内面の近傍とは、側壁内面と液体原料との間に生じる温度勾配領域(図3の「側壁側の温度勾配領域」)内であって、且つ、気泡が生じている状態において、側壁内面への気泡の付着による気化効率などの影響が実質的に無視できる程度の位置である。温度勾配領域とは、液体原料の液面又は所定の深さにおいてヒータ3、4から水平方向に離れるに連れて液体原料の温度が変化する領域である。なお、図3は、所定の深さXにおける液体原料の温度分布及びその温度勾配領域を示している。 Here, as shown in FIG. 3, the vicinity of the second heater 4 is a temperature gradient region generated between the second heater 4 and the liquid material (“temperature gradient region on the second heater side” in FIG. 3). ) And in a state where bubbles are generated, the position is such that the influence of the bubbles attached to the second heater 4 can be substantially ignored. The vicinity of the inner surface of the side wall refers to the inner surface of the side wall in the temperature gradient region (the “temperature gradient region on the side wall side” in FIG. 3) generated between the inner surface of the side wall and the liquid raw material. This is a position where the effect of vaporization efficiency due to the adhesion of bubbles to the surface can be substantially ignored. The temperature gradient region is a region where the temperature of the liquid material changes as the liquid material moves away from the heaters 3 and 4 in the horizontal direction at the liquid surface or a predetermined depth. FIG. 3 shows the temperature distribution of the liquid source at a predetermined depth X and its temperature gradient region.
 第2のヒータ4と液体原料との間に生じる温度勾配領域は、第2のヒータ4の運転開始時(加熱開始時)と加熱安定時とで異なり、運転開始時における温度勾配領域よりも加熱安定時の温度勾配領域の方が狭い。したがって、気泡発生器5を第2のヒータ4に可及的に近づけるためには、加熱安定時における側壁内面と液体原料との間に生じる温度勾配領域内に設けられることが好ましい。また、側壁内面と液体原料との間に生じる温度勾配領域は、第1のヒータ3の運転開始時(加熱開始時)と加熱安定時とで異なり、運転開始時における温度勾配領域よりも加熱安定時の温度勾配領域の方が狭い。したがって、気泡発生器5を側壁内面に可及的に近づけるためには、加熱安定時における側壁内面と液体原料との間に生じる温度勾配領域内に設けられることが好ましい。 The temperature gradient region generated between the second heater 4 and the liquid raw material is different when the operation of the second heater 4 starts (at the start of heating) and when the heating is stable, and is heated more than the temperature gradient region at the start of the operation. The stable temperature gradient region is narrower. Therefore, in order to bring the bubble generator 5 as close as possible to the second heater 4, it is preferable that the bubble generator 5 is provided in a temperature gradient region generated between the inner surface of the side wall and the liquid raw material at the time of stable heating. In addition, the temperature gradient region generated between the inner surface of the side wall and the liquid raw material is different at the start of operation of the first heater 3 (at the start of heating) and at the time of stable heating, and more stable than the temperature gradient region at the start of operation. The temperature gradient region at the time is narrower. Therefore, in order to bring the bubble generator 5 as close as possible to the inner surface of the side wall, it is preferable that the bubble generator 5 is provided in a temperature gradient region generated between the inner surface of the side wall and the liquid material at the time of stable heating.
 ガス供給管6は、液体原料容器2の上壁から内部に挿入して設けられており、本実施形態では第2のヒータ4に沿って設けられている。具体的にガス供給管6は、液体原料容器2の上壁から内部に挿入して設けられ、第2のヒータ4に沿ってその下端下方まで延びる1本の主管61と、当該主管61の下端において分岐し、液体原料容器2の径方向に延びる複数の分岐管62とからなる。 The gas supply pipe 6 is provided by being inserted into the liquid source container 2 from the upper wall, and is provided along the second heater 4 in this embodiment. Specifically, the gas supply pipe 6 is provided by being inserted from the upper wall of the liquid source container 2 into the inside, and extends along the second heater 4 to the lower end of the lower end thereof, and the lower end of the main pipe 61. And a plurality of branch pipes 62 extending in the radial direction of the liquid raw material container 2.
 主管61は、その管軸が液体原料容器2の中心軸Cと略平行となるように設けられており、分岐管62は、主管61の管軸と略直交する方向に放射状に、且つ径方向において等間隔となるように分岐している。そして、分岐管62の先端に気泡発生器5が接続されている。つまり、ガス供給管6は、第2のヒータ4の下端下側において分岐している構成としている。なお、主管61にはキャリアガスの流量を制御するためのマスフローコントローラ(MFC)8及びキャリアガスを予熱するための予熱器9が設けられている。 The main pipe 61 is provided so that its pipe axis is substantially parallel to the central axis C of the liquid source container 2, and the branch pipe 62 is radially and radially in a direction substantially perpendicular to the pipe axis of the main pipe 61. Are branched at equal intervals. The bubble generator 5 is connected to the tip of the branch pipe 62. That is, the gas supply pipe 6 is configured to be branched on the lower side below the lower end of the second heater 4. The main pipe 61 is provided with a mass flow controller (MFC) 8 for controlling the flow rate of the carrier gas and a preheater 9 for preheating the carrier gas.
 このように気泡発生器5の上部には主管61のみの配管が存在する構成となり、気泡発生器5の上部の配管構成を簡単化することができ、気泡発生器5から生じる気泡が配管に接触することを可及的に抑制することができる。 As described above, the pipe of only the main pipe 61 exists in the upper part of the bubble generator 5, so that the pipe structure of the upper part of the bubble generator 5 can be simplified, and the bubbles generated from the bubble generator 5 come into contact with the pipe. Can be suppressed as much as possible.
 また、分岐管62と気泡発生器5とは、図4に示すように、例えばVCR継手等の管継手10により接続されている。そして、この管継手10の内部に設けられる円環状の金属製のシール材(ガスケット)11の開口径を小さくすることによって、定流量器としてのオリフィスを構成している。各分岐路62と各気泡発生器5との管継手10は同一の構成であり、さらにその内部のシール材11も同一の構成である。これにより、各気泡発生器5に供給されるキャリアガスの供給流量が同一となるように構成している。 Further, as shown in FIG. 4, the branch pipe 62 and the bubble generator 5 are connected by a pipe joint 10 such as a VCR joint, for example. And the orifice as a constant flow device is comprised by making small the opening diameter of the cyclic | annular metal sealing material (gasket) 11 provided in the inside of this pipe joint 10. FIG. The pipe joints 10 of the respective branch passages 62 and the respective bubble generators 5 have the same configuration, and the sealing material 11 therein also has the same configuration. Thereby, it is comprised so that the supply flow rate of the carrier gas supplied to each bubble generator 5 may become the same.
 <本実施形態の効果>
 このように構成した本実施形態に係る液体原料気化装置100によれば、液体原料容器2の側壁及び内部中央部に第1のヒータ3及び第2のヒータ4を設けているので、液体原料容器2内に貯留された液体原料の温度分布の均一化を容易にすることができる。また、気泡発生器5を第2のヒータ4及び側壁内面の間に設けているので、第2のヒータ4及び側壁内面に気泡を接触しにくくすることができ、それらに気泡が付着することによる気泡の肥大化を防ぐことができる。また、複数の気泡発生器5を設けることによって、液体原料容器2が大型のものであっても、各気泡発生器5により生じた気泡により液体原料の攪拌効果を十分に発揮することができ、貯留された液体原料の温度分布の均一化を容易にすることができる。
<Effect of this embodiment>
According to the liquid raw material vaporization apparatus 100 according to the present embodiment configured as described above, since the first heater 3 and the second heater 4 are provided on the side wall and the inner central portion of the liquid raw material container 2, the liquid raw material container The temperature distribution of the liquid raw material stored in 2 can be made uniform easily. In addition, since the bubble generator 5 is provided between the second heater 4 and the inner surface of the side wall, it is possible to make it difficult for the bubbles to contact the second heater 4 and the inner surface of the side wall, and the bubbles adhere to them. Bubbles can be prevented from growing. Further, by providing a plurality of bubble generators 5, even if the liquid source container 2 is large, the stirring effect of the liquid source can be sufficiently exerted by the bubbles generated by each bubble generator 5, The temperature distribution of the stored liquid raw material can be made uniform easily.
 <その他の変形実施形態>
 なお、本発明は前記実施形態に限られるものではない。
<Other modified embodiments>
The present invention is not limited to the above embodiment.
 例えば、前記実施形態では、キャリアガス供給管が1つの主管と複数の分岐管とから成るものであったが、キャリアガス供給管を分岐させることなく、各気泡発生器に1つのキャリアガス供給管を設けるようにしても良い。また、複数個の気泡発生器を群として、その群毎に前記実施形態と同様のキャリアガス供給管を設けるようにしても良い。 For example, in the embodiment, the carrier gas supply pipe is composed of one main pipe and a plurality of branch pipes, but one carrier gas supply pipe is provided for each bubble generator without branching the carrier gas supply pipe. May be provided. Further, a plurality of bubble generators may be grouped, and a carrier gas supply pipe similar to that of the above embodiment may be provided for each group.
 また、キャリアガス供給管の接続位置としては、液体原料容器の上壁に限られず、側壁又は下壁であっても良い。 Further, the connection position of the carrier gas supply pipe is not limited to the upper wall of the liquid source container, and may be a side wall or a lower wall.
 さらに、前記実施形態では、キャリアガス供給管の分岐管に設ける定流量器をVCR継手内部に設けられるシール材を用いて構成しているが、別途分岐管上に定流量器を設けるようにしても良い。 Furthermore, in the said embodiment, although the constant flow device provided in the branch pipe of a carrier gas supply pipe is comprised using the sealing material provided in a VCR joint inside, it is made to provide a constant flow device separately on a branch pipe. Also good.
 加えて、図5に示すように、複数個の気泡発生器を群として、各群毎にキャリアガス供給管6A、6Bを設け、各供給管6A、6Bに切替弁Vを設けることにより、供給管6A、6Bを切り替えて液体原料を気化させるように構成しても良い。この場合、各供給管6A、6B内の圧力を測定する圧力センサPを設け、使用している一方の供給管内の圧力が所定値以上に昇圧した場合に、気泡発生器5が詰まっている等の不具合があるとして、他方の供給管に切り替えることによって気泡を発生させるようにする。なお、図5においては、各キャリアガス供給管6A、6Bは上流側で合流しており、当該合流点に圧力センサPを設けて圧力を測定する構成を示している。これならば、一方のキャリアガス供給管に設けられた気泡発生器が詰まる等の不具合が生じた場合に、他方のキャリアガス供給管に切り替えることによって長期間の運転が可能となる。 In addition, as shown in FIG. 5, by supplying a plurality of bubble generators as a group, carrier gas supply pipes 6A and 6B are provided for each group, and switching valves V are provided in the supply pipes 6A and 6B. You may comprise so that the liquid raw material may be vaporized by switching the pipes 6A and 6B. In this case, a pressure sensor P for measuring the pressure in each of the supply pipes 6A and 6B is provided, and the bubble generator 5 is clogged when the pressure in one of the supply pipes used is increased to a predetermined value or more. Therefore, bubbles are generated by switching to the other supply pipe. FIG. 5 shows a configuration in which the carrier gas supply pipes 6A and 6B merge on the upstream side and a pressure sensor P is provided at the junction to measure the pressure. In this case, when a problem such as clogging of a bubble generator provided in one carrier gas supply pipe occurs, switching to the other carrier gas supply pipe enables long-term operation.
 前記実施形態の液体材料気化装置は、複数の気泡発生器を用いて構成されているが、その他、環状(例えば円環状)をなす1つの気泡発生器を用いて第2のヒータを取り囲むように構成しても良い。 The liquid material vaporization apparatus of the above embodiment is configured using a plurality of bubble generators. In addition, a single bubble generator having an annular shape (for example, an annular shape) is used to surround the second heater. It may be configured.
 その上、前記実施形態では、4つの気泡発生器を有するものであったが、キャリアガスの流量又は液体原料容器のサイズ、形状等の構成によって気泡発生器の個数は適宜変更可能である。 In addition, in the above-described embodiment, the four bubble generators are provided. However, the number of bubble generators can be appropriately changed depending on the configuration of the flow rate of the carrier gas or the size and shape of the liquid source container.
 さらに加えて、前記実施形態では、気泡発生器を放射状に等間隔に設けるようにしているが、気泡発生器の配置態様は、液体原料容器内の構成により適宜変更可能である。 In addition, in the above embodiment, the bubble generators are provided radially at equal intervals, but the arrangement mode of the bubble generators can be changed as appropriate depending on the configuration in the liquid source container.
 また、前記実施形態の液体原料気化装置が第2のヒータを有さないものであっても液体原料を気化することができるが、液体原料容器が大型化すると気化効率が低下してしまう。一方で、液体原料容器が小型のものであれば、第1のヒータのみで液体原料を充分に気化することができる。つまり、液体原料容器が小型のものであれば、液体原料気化装置は、液体原料が貯留される液体原料容器と、前記液体原料容器の少なくとも側壁に設けられて、貯留された液体原料を加熱するためのヒータと、貯留された液体原料中に浸漬されるとともに、前記液体原料中にキャリアガスを放出してバブリングするための複数の気泡発生器と、前記気泡発生器にキャリアガスを供給するガス供給管と、を備え、複数の気泡発生器により生じる気泡が前記液体原料容器の側壁内面の近傍通過するように、複数の気泡発生器が設けられていることが望ましい。 Further, even if the liquid raw material vaporizer of the embodiment does not have the second heater, the liquid raw material can be vaporized, but if the liquid raw material container is enlarged, the vaporization efficiency is lowered. On the other hand, if the liquid material container is small, the liquid material can be sufficiently vaporized only by the first heater. That is, if the liquid source container is small, the liquid source vaporizer is provided on at least the side wall of the liquid source container in which the liquid source is stored and the liquid source container, and heats the stored liquid source And a plurality of bubble generators for immersing in the stored liquid raw material, releasing a carrier gas into the liquid raw material and bubbling, and supplying the carrier gas to the bubble generator It is desirable that a plurality of bubble generators be provided so that bubbles generated by the plurality of bubble generators pass in the vicinity of the inner surface of the side wall of the liquid raw material container.
 その他、本発明は前記実施形態に限られず、その趣旨を逸脱しない範囲で種々の変形が可能であるのは言うまでもない。 In addition, it goes without saying that the present invention is not limited to the above-described embodiment, and various modifications can be made without departing from the spirit of the present invention.
 本発明により、気泡の再結合を防止して気泡の肥大化を抑制するとともに、液体原料容器に貯留された液体原料の温度を均一にすることができる。 According to the present invention, the recombination of bubbles can be prevented to suppress the enlargement of bubbles, and the temperature of the liquid raw material stored in the liquid raw material container can be made uniform.

Claims (4)

  1.  液体原料が貯留される液体原料容器と、
     前記液体原料容器の少なくとも側壁に設けられて、貯留された液体原料を加熱するための第1のヒータと、
     前記液体原料容器の内部に設けられて、貯留された液体原料を加熱するための第2のヒータと、
     貯留された液体原料中に浸漬されるとともに、前記第2のヒータ及び側壁との間に設けられ、前記液体原料中にキャリアガスを放出してバブリングするための複数の気泡発生器と、
     前記気泡発生器にキャリアガスを供給するガス供給管と、を備える液体原料気化装置。
    A liquid source container in which the liquid source is stored;
    A first heater provided on at least a side wall of the liquid source container for heating the stored liquid source;
    A second heater provided in the liquid source container for heating the stored liquid source;
    A plurality of bubble generators that are immersed in the stored liquid raw material and provided between the second heater and the side wall, for discharging a carrier gas into the liquid raw material and bubbling;
    A liquid raw material vaporizer comprising: a gas supply pipe for supplying a carrier gas to the bubble generator.
  2.  前記複数の気泡発生器により生じる気泡が、前記液体原料容器の側壁内面の近傍及び前記第2のヒータの近傍を通過するように、前記複数の気泡発生器が設けられている請求項1記載の液体原料気化装置。 2. The plurality of bubble generators are provided so that bubbles generated by the plurality of bubble generators pass through the vicinity of the inner surface of the side wall of the liquid source container and the vicinity of the second heater. Liquid raw material vaporizer.
  3.  前記複数の気泡発生器が、前記液体原料容器の中心軸を中心として放射状に且つ等間隔に設けられている請求項1記載の液体原料気化装置。 The liquid raw material vaporizer according to claim 1, wherein the plurality of bubble generators are provided radially and equidistantly about a central axis of the liquid raw material container.
  4.  前記複数の気泡発生器が同一の構成のものであり、前記ガス供給管が、前記複数の気泡発生器に一定流量のキャリアガスを供給するための定流量器を備える請求項1記載の液体原料気化装置。 The liquid material according to claim 1, wherein the plurality of bubble generators have the same configuration, and the gas supply pipe includes a constant flow device for supplying a carrier gas having a constant flow rate to the plurality of bubble generators. Vaporizer.
PCT/JP2010/056908 2009-04-21 2010-04-19 Liquid raw material vaporizer WO2010122972A1 (en)

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