TW202419676A - Liquid material vaporizer and liquid material vaporization method - Google Patents

Liquid material vaporizer and liquid material vaporization method Download PDF

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TW202419676A
TW202419676A TW112138267A TW112138267A TW202419676A TW 202419676 A TW202419676 A TW 202419676A TW 112138267 A TW112138267 A TW 112138267A TW 112138267 A TW112138267 A TW 112138267A TW 202419676 A TW202419676 A TW 202419676A
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gas
section
liquid
liquid material
carrier gas
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西脇圭亮
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日商堀場Stec股份有限公司
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J7/00Apparatus for generating gases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B7/00Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
    • B05B7/02Spray pistols; Apparatus for discharge
    • B05B7/04Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/448Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for generating reactive gas streams, e.g. by evaporation or sublimation of precursor materials
    • 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
    • H01L21/04Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer
    • H01L21/18Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic Table or AIIIBV compounds with or without impurities, e.g. doping materials
    • H01L21/30Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26
    • H01L21/31Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26 to form insulating layers thereon, e.g. for masking or by using photolithographic techniques; After treatment of these layers; Selection of materials for these layers

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Computer Hardware Design (AREA)
  • Microelectronics & Electronic Packaging (AREA)
  • Power Engineering (AREA)
  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Chemical Vapour Deposition (AREA)

Abstract

This liquid material vaporizer comprises: a gas-liquid mixing section that mixes a liquid material and a carrier gas to generate a gas-liquid mixture; a carrier gas supply channel that supplies the carrier gas to the gas-liquid mixing section; a channel section through which the gas-liquid mixture generated in the gas-liquid mixing section flows; a vaporizer that heats and vaporizes the liquid material contained in the gas-liquid mixture that flows through the channel section; and a cooling section that cools the channel section. The cooling section is connected to the carrier gas supply channel.

Description

液體材料汽化裝置及液體材料汽化方法Liquid material vaporization device and liquid material vaporization method

本發明是有關於一種液體材料汽化裝置及液體材料汽化方法。The present invention relates to a liquid material vaporization device and a liquid material vaporization method.

在直接液體注射(Direct Liquid Injection,DLI)方式的液體材料汽化裝置(以下亦稱為「汽化器」)中,藉由噴嘴將混合有液體材料與載氣的氣液混合體噴霧至汽化室內,使液體材料汽化。為了使液體材料在汽化室內完全汽化,而利用加熱器加熱汽化室。In a direct liquid injection (DLI) liquid material vaporization device (hereinafter also referred to as a "vaporizer"), a gas-liquid mixture of liquid material and carrier gas is sprayed into a vaporization chamber through a nozzle to vaporize the liquid material. In order to completely vaporize the liquid material in the vaporization chamber, a heater is used to heat the vaporization chamber.

然而,若汽化室因加熱而成為高溫,則汽化室的熱變得容易傳導至噴霧前的氣液混合體。其結果為,擔憂氣液混合體所包含的液體材料於在汽化室內汽化之前會熱分解或變質。However, if the vaporization chamber is heated to a high temperature, the heat of the vaporization chamber becomes easily transferred to the gas-liquid mixture before spraying. As a result, there is a concern that the liquid material contained in the gas-liquid mixture will be thermally decomposed or deteriorated before being vaporized in the vaporization chamber.

就該方面而言,例如專利文獻1中揭示了一種包括將噴嘴冷卻的冷卻構造的汽化器。所述冷卻構造包括供冷媒流通的冷媒通路。作為所述冷媒,可使用水或冷卻劑。藉由冷媒在冷媒通路中流通,將噴嘴冷卻。藉此,減少汽化室的熱導致噴霧前的液體材料揮發的情況。 [現有技術文獻] [專利文獻] In this regard, for example, Patent Document 1 discloses a vaporizer including a cooling structure for cooling a nozzle. The cooling structure includes a refrigerant passage for circulating a refrigerant. Water or a coolant can be used as the refrigerant. The refrigerant is circulated in the refrigerant passage to cool the nozzle. In this way, the volatilization of the liquid material before spraying caused by the heat of the vaporization chamber is reduced. [Prior art document] [Patent document]

[專利文獻1]日本專利特開2005-109348號公報[Patent Document 1] Japanese Patent Publication No. 2005-109348

[發明所欲解決之課題][The problem that the invention wants to solve]

然而,在專利文獻1的汽化器的冷卻構造中,除了在液體材料中混合的載氣以外,需要使用將作為冷卻對象的噴嘴冷卻的專用的冷媒。因此,需要用以導入所述冷媒的設備、及在噴嘴的冷卻後將所述冷媒廢棄的設備。其結果為,有導致設置有汽化器的半導體處理裝置的大型化之虞。而且,亦有冷媒的導入及廢棄所需的設備的設置導致成本增大之虞。However, in the cooling structure of the vaporizer of Patent Document 1, in addition to the carrier gas mixed in the liquid material, a dedicated refrigerant is required to cool the nozzle to be cooled. Therefore, equipment for introducing the refrigerant and equipment for discarding the refrigerant after cooling the nozzle are required. As a result, there is a risk of increasing the size of the semiconductor processing device provided with the vaporizer. In addition, there is a risk of increasing the cost due to the installation of equipment required for introducing and discarding the refrigerant.

本發明是為了解決所述問題點而完成,其目的在於提供一種液體材料汽化裝置及液體材料汽化方法,該液體材料汽化裝置及液體材料汽化方法能夠將混合於液體材料中的載氣有效用作用以將冷卻對象冷卻的氣體,藉此,能夠抑制半導體處理裝置的大型化及成本的增大。 [解決課題之手段] The present invention is completed to solve the above-mentioned problem, and its purpose is to provide a liquid material vaporization device and a liquid material vaporization method, which can effectively use the carrier gas mixed in the liquid material to cool the cooling object, thereby suppressing the size and cost increase of the semiconductor processing equipment. [Means for solving the problem]

本發明的一方面的液體材料汽化裝置包括:氣液混合部,將液體材料與載氣混合而生成氣液混合體;載氣供給路,向所述氣液混合部供給所述載氣;流路部,供所述氣液混合部中所生成的所述氣液混合體流通;汽化部,將在所述流路部中流通的所述氣液混合體所包含的所述液體材料加熱而使其汽化;及冷卻部,將所述流路部冷卻,所述冷卻部與所述載氣供給路連通。One aspect of the present invention provides a liquid material vaporization device including: a gas-liquid mixing section for mixing a liquid material with a carrier gas to generate a gas-liquid mixture; a carrier gas supply path for supplying the carrier gas to the gas-liquid mixing section; a flow path section for circulating the gas-liquid mixture generated in the gas-liquid mixing section; a vaporization section for heating and vaporizing the liquid material contained in the gas-liquid mixture circulating in the flow path section; and a cooling section for cooling the flow path section, wherein the cooling section is connected to the carrier gas supply path.

本發明的另一方面的液體材料汽化方法包括:氣液混合體生成步驟,在氣液混合部中將液體材料與載氣混合,藉此生成氣液混合體;汽化步驟,將所述氣液混合部中所生成並經由流路部供給至汽化部的所述氣液混合體所包含的所述液體材料在所述汽化部中加熱而使其汽化;冷卻步驟,藉由所述載氣的供給將所述流路部冷卻;及載氣供給步驟,將所述冷卻步驟中冷卻所述流路部後的所述載氣經由載氣供給路供給至所述氣液混合部。 [發明的效果] Another aspect of the present invention is a method for vaporizing a liquid material, including: a gas-liquid mixture generation step, in which a liquid material is mixed with a carrier gas in a gas-liquid mixing section to generate a gas-liquid mixture; a vaporization step, in which the liquid material contained in the gas-liquid mixture generated in the gas-liquid mixing section and supplied to the vaporization section via a flow path section is heated in the vaporization section to vaporize the liquid material; a cooling step, in which the flow path section is cooled by supplying the carrier gas; and a carrier gas supply step, in which the carrier gas after cooling the flow path section in the cooling step is supplied to the gas-liquid mixing section via a carrier gas supply path. [Effect of the invention]

根據本發明,能夠將混合於液體材料中的載氣有效用作用以將冷卻對象冷卻的氣體,藉此,能夠抑制設置有液體材料汽化裝置的半導體處理裝置的大型化及成本的增大。According to the present invention, the carrier gas mixed in the liquid material can be effectively used as a gas for cooling the cooling object, thereby suppressing the increase in size and cost of a semiconductor processing apparatus provided with a liquid material vaporization device.

以下,參照圖式對本發明的例示性的實施方式進行說明。Hereinafter, exemplary embodiments of the present invention will be described with reference to the drawings.

〔1.液體材料汽化裝置〕 圖1是示意性地表示本實施方式的液體材料汽化裝置1的概略構造的截面圖。液體材料汽化裝置1例如設置於半導體製造裝置(未圖示)。液體材料汽化裝置1包括流量控制閥2、汽化部3、連接部4、及冷卻部5。 [1. Liquid material vaporization device] FIG. 1 is a cross-sectional view schematically showing the general structure of a liquid material vaporization device 1 of the present embodiment. The liquid material vaporization device 1 is provided in, for example, a semiconductor manufacturing device (not shown). The liquid material vaporization device 1 includes a flow control valve 2, a vaporization section 3, a connection section 4, and a cooling section 5.

(1-1.流量控制閥) 流量控制閥2是控制所使用的流體(氣體或液體)的流量的機構,例如構成質量流量控制器(流量控制裝置)的一部分。流量控制閥2例如由常開型構成,包括本體區塊21、支持區塊22、及致動器23。 (1-1. Flow control valve) The flow control valve 2 is a mechanism for controlling the flow rate of the fluid (gas or liquid) used, for example, constituting a part of a mass flow controller (flow control device). The flow control valve 2 is, for example, a normally open type, and includes a body block 21, a support block 22, and an actuator 23.

本體區塊21由不鏽鋼等金屬素材所形成。本體區塊21包括閥座面21S。相對於閥座面21S,下文所述的閥體24的落座面24S接觸分離(接觸或分離)。The body block 21 is formed of a metal material such as stainless steel. The body block 21 includes a valve seat surface 21S. With respect to the valve seat surface 21S, a seat surface 24S of a valve body 24 described below is in contact with or separated from the valve seat surface 21S.

在本體區塊21形成有液體材料供給路21a、載氣供給路21b、及氣液混合體排出路21c。液體材料供給路21a是將成為汽化部3中所汽化的對象的液體材料LQ供給至下文所述的氣液混合部29的流路。載氣供給路21b是向氣液混合部29供給載氣CG的流路。作為載氣CG,例如可使用氮氣、氬氣等惰性氣體。氣液混合體排出路21c是將氣液混合部29中所生成的氣液混合體MG排出的流路。所述氣液混合體MG是液體材料LQ與載氣CG的混合體。載氣供給路21b及氣液混合體排出路21c經由設置於閥座面21S的連通路21d連通。A liquid material supply path 21a, a carrier gas supply path 21b, and a gas-liquid mixture discharge path 21c are formed in the main body block 21. The liquid material supply path 21a is a flow path for supplying the liquid material LQ to be vaporized in the vaporization section 3 to the gas-liquid mixing section 29 described below. The carrier gas supply path 21b is a flow path for supplying the carrier gas CG to the gas-liquid mixing section 29. As the carrier gas CG, for example, an inert gas such as nitrogen and argon can be used. The gas-liquid mixture discharge path 21c is a flow path for discharging the gas-liquid mixture MG generated in the gas-liquid mixing section 29. The gas-liquid mixture MG is a mixture of the liquid material LQ and the carrier gas CG. The carrier gas supply path 21b and the gas-liquid mixture discharge path 21c are connected via a connecting path 21d provided on the valve seat surface 21S.

支持區塊22包括閥體24。閥體24是相對於本體區塊21的閥座面21S沿著接觸分離方向(例如上下方向)移動的移動體,包括與閥座面21S接觸的落座面24S。閥體24在與所述接觸分離方向交叉的方向(例如水平方向)上隔著隔膜25而由支持體26所支持。支持體26例如藉由螺栓緊固於本體區塊21。The support block 22 includes a valve body 24. The valve body 24 is a movable body that moves along the contact separation direction (e.g., up and down direction) relative to the valve seat surface 21S of the main body block 21, and includes a seating surface 24S that contacts the valve seat surface 21S. The valve body 24 is supported by a support body 26 via a diaphragm 25 in a direction intersecting the contact separation direction (e.g., horizontal direction). The support body 26 is fastened to the main body block 21, for example, by bolts.

致動器23是使閥體24沿著所述接觸分離方向移動的驅動部。致動器23例如包括壓電堆231。壓電堆231是將藉由電壓施加而膨脹變形的壓電元件積層多塊所形成。壓電堆231收容於收容體232內,經由真球27及柱塞28對閥體24施加推壓力。所述收容體232被固定於支持體26。The actuator 23 is a driving part that moves the valve body 24 along the contact separation direction. The actuator 23 includes, for example, a piezoelectric stack 231. The piezoelectric stack 231 is formed by laminating a plurality of piezoelectric elements that expand and deform when voltage is applied. The piezoelectric stack 231 is housed in a housing 232, and applies a pushing force to the valve body 24 via a ball 27 and a plunger 28. The housing 232 is fixed to a support 26.

而且,流量控制閥2進而包括氣液混合部29。氣液混合部29將液體材料LQ與載氣CG混合,生成所述氣液混合體MG。此種液體材料LQ與載氣CG的混合是在本體區塊21的閥座面21S與閥體24的落座面24S之間的空間中進行。此處將所述空間稱為氣液混合室29a。因此,氣液混合部29包括所述氣液混合室29a。Moreover, the flow control valve 2 further includes a gas-liquid mixing section 29. The gas-liquid mixing section 29 mixes the liquid material LQ with the carrier gas CG to generate the gas-liquid mixture MG. The mixing of the liquid material LQ and the carrier gas CG is performed in the space between the valve seat surface 21S of the main body block 21 and the seat surface 24S of the valve body 24. The space is referred to as a gas-liquid mixing chamber 29a. Therefore, the gas-liquid mixing section 29 includes the gas-liquid mixing chamber 29a.

氣液混合室29a是閥座面21S與落座面24S之間的空間,閥座面21S及落座面24S形成所述氣液混合室29a。因此,可認為氣液混合部29是包括形成氣液混合室29a的閥座面21S及落座面24S而構成。The gas-liquid mixing chamber 29a is a space between the valve seat surface 21S and the seat surface 24S, and the valve seat surface 21S and the seat surface 24S form the gas-liquid mixing chamber 29a. Therefore, it can be considered that the gas-liquid mixing portion 29 is composed of the valve seat surface 21S and the seat surface 24S that form the gas-liquid mixing chamber 29a.

在所述構造中,在未對壓電堆231施加電壓的狀態下,以閥開度(閥座面21S與落座面24S之間的間隙)成為規定值的方式進行設定。在該狀態下,藉由未圖示的賦能構件將閥體24與柱塞28一起推向第一方向。所述第一方向例如為落座面24S相對於閥座面21S而分離的方向(例如圖1中為上向)。In the above structure, the valve opening (gap between the valve seat surface 21S and the seat surface 24S) is set to a predetermined value when no voltage is applied to the piezoelectric stack 231. In this state, the valve body 24 and the plunger 28 are pushed in a first direction by an enabling member (not shown). The first direction is, for example, a direction in which the seat surface 24S is separated from the valve seat surface 21S (for example, upward in FIG. 1 ).

若對壓電堆231施加電壓,則壓電堆231伸長。由此,壓電堆231抵抗所述賦能構件的施加力,經由真球27及柱塞28將閥體24推向與第一方向相反的第二方向(例如下向)。並且最終使閥體24的落座面24S落座於閥座面21S。If voltage is applied to the piezoelectric stack 231, the piezoelectric stack 231 will extend. As a result, the piezoelectric stack 231 resists the applied force of the energy-enabling member, and pushes the valve body 24 in a second direction (e.g., downward) opposite to the first direction through the ball 27 and the plunger 28. Finally, the seat surface 24S of the valve body 24 is seated on the valve seat surface 21S.

在落座面24S落座於閥座面21S之前的狀態、即在閥座面21S與落座面24S之間形成有間隙的狀態下,液體材料LQ經由液體材料供給路21a被供給至氣液混合部29(氣液混合室29a),載氣CG經由載氣供給路21b被供給至氣液混合部29。在氣液混合部29中,將液體材料LQ與載氣CG混合而生成氣液混合體MG後,所生成的氣液混合體MG經由氣液混合體排出路21c排出至連接部4,並流向汽化部3。In a state before the seating surface 24S is seated on the valve seat surface 21S, that is, in a state in which a gap is formed between the valve seat surface 21S and the seating surface 24S, the liquid material LQ is supplied to the gas-liquid mixing section 29 (gas-liquid mixing chamber 29a) through the liquid material supply path 21a, and the carrier gas CG is supplied to the gas-liquid mixing section 29 through the carrier gas supply path 21b. In the gas-liquid mixing section 29, after the liquid material LQ and the carrier gas CG are mixed to generate a gas-liquid mixture MG, the generated gas-liquid mixture MG is discharged to the connecting section 4 through the gas-liquid mixture discharge path 21c, and flows to the vaporizing section 3.

一方面,若落座面24S落座於閥座面21S,則液體材料LQ的流量成為零。另一方面,載氣CG自載氣供給路21b起,經由設置於閥座面21S的連通路21d流向氣液混合體排出路21c。即,在落座面24S落座於閥座面21S的狀態下,僅載氣CG在氣液混合體排出路21c中流動並被排出。再者,亦可設為在落座面24S落座於閥座面21S的狀態下,(與液體材料LQ同樣地)載氣CG的流量亦成為零的構造(即未流通液體材料LQ及載氣CG的構造)。On the one hand, if the seating surface 24S is seated on the valve seat surface 21S, the flow rate of the liquid material LQ becomes zero. On the other hand, the carrier gas CG flows from the carrier gas supply path 21b to the gas-liquid mixture discharge path 21c via the connecting path 21d provided on the valve seat surface 21S. That is, when the seating surface 24S is seated on the valve seat surface 21S, only the carrier gas CG flows in the gas-liquid mixture discharge path 21c and is discharged. Furthermore, it is also possible to have a structure in which the flow rate of the carrier gas CG also becomes zero (similar to the liquid material LQ) when the seating surface 24S is seated on the valve seat surface 21S (i.e., a structure in which the liquid material LQ and the carrier gas CG do not flow).

如上所述,藉由利用致動器23使閥體24移動的構造,可對致動器23施加與所需的閥開度相應的電壓,而實現所述閥開度。藉此,能夠適當地調整(控制)供給至氣液混合部29而與載氣CG混合、並與載氣CG一起被排出的液體材料LQ的流量。As described above, by using the actuator 23 to move the valve body 24, a voltage corresponding to the desired valve opening can be applied to the actuator 23 to achieve the valve opening. In this way, the flow rate of the liquid material LQ supplied to the gas-liquid mixing section 29, mixed with the carrier gas CG, and discharged together with the carrier gas CG can be appropriately adjusted (controlled).

(1-2.汽化部) 汽化部3將自流量控制閥2的氣液混合體排出路21c排出的氣液混合體MG所包含的液體材料LQ加熱而使其汽化。此種汽化部3包括汽化室31、及噴嘴N。汽化室31是使氣液混合體MG所包含的液體材料LQ汽化的腔室,藉由未圖示的加熱器進行加熱。噴嘴N位於汽化室31的上游側,與汽化室31連通,將所述氣液混合體MG噴霧至汽化室31內。 (1-2. Vaporization section) The vaporization section 3 heats the liquid material LQ contained in the gas-liquid mixture MG discharged from the gas-liquid mixture discharge passage 21c of the flow control valve 2 to vaporize it. Such a vaporization section 3 includes a vaporization chamber 31 and a nozzle N. The vaporization chamber 31 is a chamber for vaporizing the liquid material LQ contained in the gas-liquid mixture MG, and is heated by a heater not shown. The nozzle N is located on the upstream side of the vaporization chamber 31, communicates with the vaporization chamber 31, and sprays the gas-liquid mixture MG into the vaporization chamber 31.

(1-3.連接部) 連接部4將流量控制閥2的氣液混合體排出路21c與汽化部3連接。在圖1的構造中,連接部4包括連接管41而構成。連接管41是將氣液混合體排出路21c與噴嘴N連接的環狀的管。連接部4由不鏽鋼等金屬材料所形成。 (1-3. Connecting part) The connecting part 4 connects the gas-liquid mixture discharge path 21c of the flow control valve 2 with the vaporizing part 3. In the structure of FIG1 , the connecting part 4 includes a connecting tube 41. The connecting tube 41 is a ring-shaped tube that connects the gas-liquid mixture discharge path 21c with the nozzle N. The connecting part 4 is formed of a metal material such as stainless steel.

此處,流量控制閥2的氣液混合體排出路21c與所述連接部4構成供氣液混合部29中所生成的氣液混合體MG流通的流路部FP。即,流路部FP是包括氣液混合體排出路21c、及連接部4而構成。因此,亦可認為所述汽化部3將在流路部FP中流通的氣液混合體MG所包含的液體材料LQ加熱而使其汽化。Here, the gas-liquid mixture discharge passage 21c of the flow control valve 2 and the connection portion 4 constitute a flow passage portion FP through which the gas-liquid mixture MG generated in the gas-liquid mixing portion 29 flows. That is, the flow passage portion FP is composed of the gas-liquid mixture discharge passage 21c and the connection portion 4. Therefore, it can also be considered that the vaporization portion 3 heats and vaporizes the liquid material LQ contained in the gas-liquid mixture MG flowing in the flow passage portion FP.

冷卻部5將流路部FP冷卻。尤其是冷卻部5將流路部FP所包括的連接部4冷卻。此種冷卻部5是包括殼體51、導入口52、及導出口53而構成。The cooling unit 5 cools the flow path unit FP. In particular, the cooling unit 5 cools the connection unit 4 included in the flow path unit FP. The cooling unit 5 includes a housing 51, an inlet 52, and an outlet 53.

殼體51覆蓋連接部4的周圍。在本實施方式中,殼體51位於連接管41的周圍,與連接管41一體地形成。即,殼體51及連接管41是由以殼體51作為外管、以連接管41作為內管的雙配管所構成。The housing 51 covers the periphery of the connection portion 4. In the present embodiment, the housing 51 is located around the connection pipe 41 and is formed integrally with the connection pipe 41. That is, the housing 51 and the connection pipe 41 are formed of a double pipe having the housing 51 as an outer pipe and the connection pipe 41 as an inner pipe.

導入口52是向殼體51內導入載氣CG的埠(開口部)。作為導入殼體51內的載氣CG,使用與流量控制閥2中混合於液體材料LQ中的載氣CG相同的氣體。導出口53是將載氣CG自殼體51導出(排出)的埠(開口部)。導入口52相對於導出口53而位於汽化部3側。The inlet 52 is a port (opening) for introducing the carrier gas CG into the housing 51. As the carrier gas CG introduced into the housing 51, the same gas as the carrier gas CG mixed in the liquid material LQ in the flow control valve 2 is used. The outlet 53 is a port (opening) for leading (discharging) the carrier gas CG from the housing 51. The inlet 52 is located on the vaporization section 3 side relative to the outlet 53.

在冷卻部5的殼體51內,藉由使載氣CG自導入口52流向導出口53,能夠將殼體51所覆蓋的連接部4(連接管41)冷卻。例如,即便汽化部3成為200℃左右的高溫,藉由將設置液體材料汽化裝置1的環境溫度(例如室溫程度)的載氣CG導入冷卻部5,亦能夠將連接部4冷卻。因此,即便汽化部3成為高溫,汽化部3的熱亦難以經由連接部4傳導至上游側(流量控制閥2的氣液混合部29側)。藉此,在將氣液混合體MG供給至汽化部3之前,可降低氣液混合體MG所包含的液體材料LQ熱分解及變質的擔憂。In the housing 51 of the cooling section 5, by allowing the carrier gas CG to flow from the inlet 52 to the outlet 53, the connecting section 4 (connecting tube 41) covered by the housing 51 can be cooled. For example, even if the vaporization section 3 reaches a high temperature of about 200°C, the connecting section 4 can be cooled by introducing the carrier gas CG of the ambient temperature (e.g., room temperature) of the liquid material vaporization device 1 into the cooling section 5. Therefore, even if the vaporization section 3 reaches a high temperature, the heat of the vaporization section 3 is difficult to be transferred to the upstream side (the gas-liquid mixing section 29 side of the flow control valve 2) through the connecting section 4. Thereby, before the gas-liquid mixture MG is supplied to the vaporization section 3, the concern about the thermal decomposition and deterioration of the liquid material LQ contained in the gas-liquid mixture MG can be reduced.

尤其是在使用蒸氣壓低的材料(例如鍶)作為液體材料LQ的情況下,為了在汽化部3中使液體材料LQ蒸發,需要使汽化部3的溫度更高。因此,為了減少液體材料LQ的熱分解等,藉由冷卻部5冷卻連接部4的本實施方式的構造尤其在使用蒸氣壓低的材料作為液體材料LQ的情況下有效。In particular, when a material with a low vapor pressure (e.g., strontium) is used as the liquid material LQ, the temperature of the vaporization section 3 needs to be increased in order to evaporate the liquid material LQ in the vaporization section 3. Therefore, in order to reduce thermal decomposition of the liquid material LQ, the structure of the present embodiment in which the connection section 4 is cooled by the cooling section 5 is particularly effective when a material with a low vapor pressure is used as the liquid material LQ.

在本實施方式中,如圖1所示,冷卻部5與流量控制閥2的載氣供給路21b連通。例如藉由經由未圖示的凸緣將冷卻部5與流量控制閥2的本體區塊21螺栓緊固,能夠使冷卻部5與載氣供給路21b連通。尤其是藉由所述螺栓緊固,冷卻部5的殼體51經由導出口53而與載氣供給路21b連通。In the present embodiment, as shown in FIG1 , the cooling unit 5 is connected to the carrier gas supply path 21 b of the flow control valve 2. For example, by bolting the cooling unit 5 to the body block 21 of the flow control valve 2 via a flange (not shown), the cooling unit 5 can be connected to the carrier gas supply path 21 b. In particular, by bolting, the housing 51 of the cooling unit 5 is connected to the carrier gas supply path 21 b via the guide port 53.

(2.液體材料汽化方法) 圖2是表示使用所述構造的液體材料汽化裝置1使液體材料LQ汽化的液體材料汽化方法的各步驟的流程的流程圖。以下,基於圖1及圖2對本實施方式的液體材料汽化方法進行說明。 (2. Liquid material vaporization method) FIG. 2 is a flow chart showing the flow of each step of a liquid material vaporization method for vaporizing liquid material LQ using the liquid material vaporization device 1 of the above structure. The liquid material vaporization method of this embodiment is described below based on FIG. 1 and FIG. 2 .

首先,向冷卻部5導入載氣CG(S1)。更詳細而言,自冷卻部5的導入口52向殼體51內導入載氣CG。藉此,開始利用冷卻部5將流路部FP(尤其是連接部4)冷卻(S2:冷卻步驟)。導入冷卻部5並冷卻連接部4後的載氣CG經由載氣供給路21b被供給至氣液混合部29(S3:載氣供給步驟)。另一方面,液體材料LQ經由液體材料供給路21a被供給至氣液混合部29(S4:液體材料供給步驟)。First, the carrier gas CG is introduced into the cooling section 5 (S1). More specifically, the carrier gas CG is introduced into the housing 51 from the inlet 52 of the cooling section 5. Thereby, the cooling of the flow path section FP (especially the connecting section 4) by the cooling section 5 begins (S2: cooling step). The carrier gas CG introduced into the cooling section 5 and after cooling the connecting section 4 is supplied to the gas-liquid mixing section 29 via the carrier gas supply path 21b (S3: carrier gas supply step). On the other hand, the liquid material LQ is supplied to the gas-liquid mixing section 29 via the liquid material supply path 21a (S4: liquid material supply step).

在氣液混合部29中,將液體材料LQ與載氣CG混合,藉此生成氣液混合體MG(S5:氣液混合體生成步驟)。In the gas-liquid mixing section 29 , the liquid material LQ and the carrier gas CG are mixed to generate a gas-liquid mixture MG ( S5 : gas-liquid mixture generating step).

氣液混合部29中所生成的氣液混合體MG經由氣液混合體排出路21c被排出至連接部4(連接管41)(S6:排出步驟)。然後,經由氣液混合體排出路21c被排出、並穿過連接部4而供給至汽化部3的氣液混合體MG所包含的液體材料LQ被汽化部3加熱而汽化(S7:汽化步驟)。The gas-liquid mixture MG generated in the gas-liquid mixing section 29 is discharged to the connecting section 4 (connecting tube 41) through the gas-liquid mixture discharge path 21c (S6: discharge step). Then, the liquid material LQ contained in the gas-liquid mixture MG discharged through the gas-liquid mixture discharge path 21c and supplied to the vaporizing section 3 through the connecting section 4 is heated by the vaporizing section 3 and vaporized (S7: vaporization step).

繼而,停止向氣液混合部29供給液體材料LQ(S8)。再者,S8視需要進行即可。繼而,在繼續進行汽化部3中使液體材料LQ汽化的處理的情況下(S9中為是),返回S4,重複進行S4之後的處理(由於一直進行S3)。再者,在流量控制閥2中,於在落座面24S落座於閥座面21S的狀態下載氣CG的流量成為零的構造中,自S9移行至S3,重複S3之後的處理即可。Then, the supply of the liquid material LQ to the gas-liquid mixing section 29 is stopped (S8). Furthermore, S8 may be performed as needed. Then, in the case of continuing the process of vaporizing the liquid material LQ in the vaporizing section 3 (Yes in S9), the process returns to S4 and the process after S4 is repeated (since S3 is always performed). Furthermore, in the flow control valve 2, in the structure where the flow rate of the carrier gas CG becomes zero in the state where the seating surface 24S is seated on the valve seat surface 21S, the process moves from S9 to S3 and the process after S3 is repeated.

另一方面,在不繼續進行所述處理的情況下(S9中為否),停止向冷卻部5導入載氣CG(S10),結束冷卻部5對連接部4的冷卻(S11),並結束一系列處理。On the other hand, when the above-mentioned process is not to be continued (No in S9), the introduction of the carrier gas CG into the cooling section 5 is stopped (S10), the cooling of the connecting section 4 by the cooling section 5 is terminated (S11), and a series of processes are terminated.

(3.效果) 如以上所述,在本實施方式中,冷卻部5與流量控制閥2的載氣供給路21b連通。因此,能夠將流量控制閥2中混合於液體材料LQ中的載氣CG自冷卻部5經由載氣供給路21b供給至氣液混合部29(參照S2、S3)。即,亦可利用混合於液體材料LQ中的載氣CG作為冷卻部5中用以冷卻流路部FP(尤其是連接部4)的氣體。藉此,除了混合於液體材料LQ中的載氣CG以外,無需準備冷卻流路部FP的專用的冷媒。因此,不需要用以導入所述冷媒的設備,進而亦不需要在冷卻後將所述冷媒廢棄的設備。其結果為,能夠抑制設置有液體材料汽化裝置1的半導體處理裝置的大型化,並且能夠抑制所述設備的設置引起的成本的增大。而且,由於不使用冷卻專用的冷媒,故而亦不會發生因所述冷媒的廢棄引起的浪費。 (3. Effect) As described above, in the present embodiment, the cooling section 5 is connected to the carrier gas supply path 21b of the flow control valve 2. Therefore, the carrier gas CG mixed in the liquid material LQ in the flow control valve 2 can be supplied from the cooling section 5 to the gas-liquid mixing section 29 via the carrier gas supply path 21b (refer to S2, S3). That is, the carrier gas CG mixed in the liquid material LQ can also be used as the gas for cooling the flow path section FP (especially the connecting section 4) in the cooling section 5. Thereby, in addition to the carrier gas CG mixed in the liquid material LQ, there is no need to prepare a dedicated refrigerant for cooling the flow path section FP. Therefore, there is no need for equipment for introducing the refrigerant, and further, there is no need for equipment for discarding the refrigerant after cooling. As a result, the size of the semiconductor processing device equipped with the liquid material vaporization device 1 can be suppressed, and the increase in cost caused by the installation of the equipment can be suppressed. Moreover, since a refrigerant dedicated to cooling is not used, waste caused by the disposal of the refrigerant will not occur.

而且,藉由流路部FP的冷卻使用載氣CG,而利用汽化部3的熱將載氣CG預熱。因此,在利用汽化部3使自冷卻部5經由載氣供給路21b向氣液混合部29供給載氣CG並與液體材料LQ混合後的氣液混合體MG汽化之前,可使液體材料LQ升溫至(在不發生熱分解等的溫度範圍內)容易汽化的溫度。藉此,亦可期待汽化部3中的液體材料LQ的汽化性能的提高。Furthermore, the carrier gas CG is used by cooling the flow path portion FP, and the carrier gas CG is preheated by the heat of the vaporization portion 3. Therefore, before the gas-liquid mixture MG after the carrier gas CG is supplied from the cooling portion 5 to the gas-liquid mixing portion 29 via the carrier gas supply path 21b and mixed with the liquid material LQ is vaporized by the vaporization portion 3, the liquid material LQ can be heated to a temperature that is easy to vaporize (within a temperature range where thermal decomposition, etc. does not occur). Thereby, it is also expected that the vaporization performance of the liquid material LQ in the vaporization portion 3 can be improved.

而且,在本實施方式中,由於殼體51覆蓋流路部FP的連接部4的周圍,故而在連接部4的周圍形成封閉的空間。由於載氣CG在該空間內流動,故而可減少開放空間中會發生的載氣CG的擴散。藉此,可減小利用載氣CG進行的冷卻的損失、及載氣CG的無用的消耗。而且,由於殼體51與載氣供給路21b連通,故而可將在殼體51內流通並冷卻連接部4後的載氣CG經由載氣供給路21b確實地供給至氣液混合部29。Moreover, in the present embodiment, since the shell 51 covers the periphery of the connecting portion 4 of the flow path portion FP, a closed space is formed around the connecting portion 4. Since the carrier gas CG flows in this space, the diffusion of the carrier gas CG that would occur in an open space can be reduced. Thereby, the loss of cooling using the carrier gas CG and the useless consumption of the carrier gas CG can be reduced. Moreover, since the shell 51 is connected to the carrier gas supply path 21b, the carrier gas CG that has circulated in the shell 51 and cooled the connecting portion 4 can be reliably supplied to the gas-liquid mixing portion 29 via the carrier gas supply path 21b.

而且,如圖1所示,載氣供給路21b與冷卻部5的導出口53連接。在該構造中,可將自冷卻部5的導入口52導入殼體51的內部的載氣CG經由導出口53供給至載氣供給路21b。即,能夠確實地實現殼體51與載氣供給路21b連通的構造。Moreover, as shown in FIG1 , the carrier gas supply path 21b is connected to the outlet 53 of the cooling unit 5. In this structure, the carrier gas CG introduced into the interior of the housing 51 from the inlet 52 of the cooling unit 5 can be supplied to the carrier gas supply path 21b via the outlet 53. That is, the structure in which the housing 51 and the carrier gas supply path 21b are connected can be realized reliably.

尤其是在如圖1般導入口52相對於導出口53而位於汽化部3側的構造中,在S2的冷卻步驟中,能夠藉由在殼體51的內部使載氣CG自靠近汽化部3一側(在連接部4中流通的氣液混合體MG的流動方向的下游側)流向遠離汽化部3一側(氣液混合體MG的流動方向的上游側)而將連接部4冷卻。In particular, in the structure in which the inlet 52 is located on the side of the vaporization section 3 relative to the outlet 53 as shown in Figure 1, in the cooling step of S2, the connecting section 4 can be cooled by allowing the carrier gas CG to flow from the side close to the vaporization section 3 (the downstream side of the flow direction of the gas-liquid mixture MG flowing in the connecting section 4) to the side far from the vaporization section 3 (the upstream side of the flow direction of the gas-liquid mixture MG) inside the shell 51.

藉此,在連接部4中,能夠先於上游側(優先)將汽化部3的熱最容易傳導的下游側效率良好地冷卻。其結果為,可確實地使汽化部3的熱難以經由連接部4傳導至上游側,從而確實地降低在汽化部3中的汽化前液體材料LQ熱分解及變質的擔憂。Thus, in the connection portion 4, the downstream side, to which the heat of the vaporization portion 3 is most easily transferred, can be efficiently cooled before the upstream side (with priority). As a result, it is possible to reliably make it difficult for the heat of the vaporization portion 3 to be transferred to the upstream side via the connection portion 4, thereby reliably reducing the concern about thermal decomposition and deterioration of the pre-vaporization liquid material LQ in the vaporization portion 3.

再者,導入口52可相對於導出口53而位於汽化部3的相反側。但在該位置關係下,需要將連通導出口53與載氣供給路21b的流路形成為較長。Furthermore, the introduction port 52 may be located on the opposite side of the vaporization portion 3 relative to the introduction port 53. However, in this positional relationship, the flow path connecting the introduction port 53 and the carrier gas supply path 21b needs to be formed to be relatively long.

(4.關於導入口的理想的位置) 圖3是以與連接部4(連接管41)中的氣液混合體MG的流動方向垂直的截面切斷冷卻部5時的截面圖。如同圖所示,較理想為冷卻部5的導入口52在所述截面內位於與針對殼體51的外周面51a的切線T重合的位置。再者,殼體51的外周面51a是隔著空隙覆蓋連接部4的圓筒狀的連接管41的外周面41a的圓筒狀的面。 (4. Ideal position of the inlet) Fig. 3 is a cross-sectional view of the cooling section 5 cut at a section perpendicular to the flow direction of the gas-liquid mixture MG in the connecting section 4 (connecting tube 41). As shown in the figure, it is ideal that the inlet 52 of the cooling section 5 is located in the cross section at a position that overlaps with the tangent T to the outer peripheral surface 51a of the shell 51. The outer peripheral surface 51a of the shell 51 is a cylindrical surface that covers the outer peripheral surface 41a of the cylindrical connecting tube 41 of the connecting section 4 with a gap.

在該構造中,自殼體51的外周面51a的切線T的方向起,經由導入口52將載氣CG導入殼體51內。藉此,在殼體51內,容易使載氣CG繞著連接部4回轉流動。藉由載氣CG的回轉,能夠利用載氣CG沿著周方向包裹住連接部4進行冷卻,因此能夠提高連接部4的冷卻效率。In this structure, the carrier gas CG is introduced into the housing 51 through the inlet 52 from the direction of the tangent line T of the outer peripheral surface 51a of the housing 51. As a result, the carrier gas CG can be easily caused to swirl around the connecting portion 4 in the housing 51. By the rotation of the carrier gas CG, the connecting portion 4 can be cooled by the carrier gas CG in the circumferential direction, thereby improving the cooling efficiency of the connecting portion 4.

根據以上,在包括圖3所示的冷卻部5的構造中,在S2的冷卻步驟中,可認為在所述截面內,藉由使載氣CG自覆蓋連接部4的周圍的殼體51的外周面51a的切線T的方向流至殼體51內,而將連接部4冷卻,藉此可獲得提高連接部4的冷卻效率的效果。Based on the above, in the structure including the cooling part 5 shown in Figure 3, in the cooling step of S2, it can be considered that within the cross-section, the connecting part 4 is cooled by allowing the carrier gas CG to flow from the direction of the tangent T of the outer peripheral surface 51a of the shell 51 covering the surrounding of the connecting part 4 into the shell 51, thereby achieving the effect of improving the cooling efficiency of the connecting part 4.

〔2.液體材料汽化裝置的另一構造〕 圖4是示意性地表示本實施方式的液體材料汽化裝置1的另一構造的截面圖。圖4的液體材料汽化裝置1除了冷卻部5的殼體51包括螺旋狀的氣體流路51P的方面以外,為與圖1同樣的構造。 [2. Another structure of the liquid material vaporization device] FIG. 4 is a cross-sectional view schematically showing another structure of the liquid material vaporization device 1 of the present embodiment. The liquid material vaporization device 1 of FIG. 4 has the same structure as FIG. 1 except that the housing 51 of the cooling unit 5 includes a spiral gas flow path 51P.

氣體流路51P是在殼體51內以螺旋狀形成於連接部4(連接管41)的周圍的流路。包括此種氣體流路51P的殼體51例如由多個分割殼體構成殼體51,可藉由利用焊接或螺栓緊固將各分割殼體貼合而實現。螺旋狀的氣體流路51P分別與所述導入口52及導出口53連通。The gas flow path 51P is a flow path formed in a spiral shape around the connection portion 4 (connection pipe 41) in the housing 51. The housing 51 including such a gas flow path 51P is formed by, for example, a plurality of divided housings, and can be realized by bonding the divided housings together by welding or bolting. The spiral gas flow path 51P is connected to the inlet 52 and the outlet 53, respectively.

在圖4的構造中,若將載氣CG自導入口52導入殼體51內,則載氣CG在殼體51內沿著螺旋狀的氣體流路51P以螺旋狀在連接部4的周圍流通。藉此,能夠利用載氣CG沿著周方向包裹住連接部4進行冷卻,因此能夠提高連接部4的冷卻效率。In the structure of Fig. 4, when the carrier gas CG is introduced into the housing 51 from the inlet 52, the carrier gas CG flows in a spiral shape around the connecting portion 4 along the spiral gas flow path 51P in the housing 51. In this way, the connecting portion 4 can be cooled by wrapping it with the carrier gas CG in the circumferential direction, thereby improving the cooling efficiency of the connecting portion 4.

根據以上,在圖4的構造中,在S2的冷卻步驟中,可認為在覆蓋連接部4的周圍的殼體51內,藉由使載氣CG在形成於連接部4的周圍的螺旋狀的氣體流路51P中流通,而將連接部4冷卻,藉此可獲得提高連接部4的冷卻效率的效果。Based on the above, in the structure of Figure 4, in the cooling step of S2, it can be considered that in the shell 51 covering the connection part 4, the connection part 4 is cooled by allowing the carrier gas CG to flow in the spiral gas flow path 51P formed around the connection part 4, thereby achieving the effect of improving the cooling efficiency of the connection part 4.

〔3.液體材料汽化裝置的又一構造〕 圖5是示意性地表示本實施方式的液體材料汽化裝置1的又一構造的截面圖。圖5的液體材料汽化裝置1除了冷卻部5在殼體51內包括散熱片54的方面以外,為與圖1同樣的構造。 [3. Another structure of the liquid material vaporization device] FIG. 5 is a cross-sectional view schematically showing another structure of the liquid material vaporization device 1 of the present embodiment. The liquid material vaporization device 1 of FIG. 5 has the same structure as FIG. 1 except that the cooling unit 5 includes a heat sink 54 in the housing 51.

散熱片54是平板狀的散熱板,在殼體51內設置多個。各散熱片54例如藉由焊接而與連接部4(連接管41)的外周面41a(參照圖3)連結。而且,各散熱片54沿著殼體51內連接部4延伸的方向以規定的間隔排列配置於外周面41a上。各散熱片54可由與連接部4相同的金屬材料所構成,亦可由熱導率較構成連接部4的金屬更高的金屬材料(例如鋁、銅或該些的合金)所構成。The heat sink 54 is a flat heat sink, and a plurality of them are provided in the housing 51. Each heat sink 54 is connected to the outer peripheral surface 41a (refer to FIG. 3 ) of the connection portion 4 (connection pipe 41) by welding, for example. Moreover, each heat sink 54 is arranged on the outer peripheral surface 41a at a predetermined interval along the direction in which the connection portion 4 extends in the housing 51. Each heat sink 54 can be made of the same metal material as the connection portion 4, or can be made of a metal material having a higher thermal conductivity than the metal constituting the connection portion 4 (for example, aluminum, copper, or an alloy thereof).

藉由在殼體51內設置與連接部4的外周面41a連結的多個散熱片54,實質上等效於將連接部4的外周面41a的表面積增加與多個散熱片54的表面積相應的量的構造。因此,在殼體51內,使載氣CG不僅與連接部4的外周面41a接觸,而且與表面積大的散熱片54接觸,而能夠使連接部4效率良好地散熱。即,能夠提高連接部4的冷卻效率。By providing a plurality of heat sinks 54 connected to the outer peripheral surface 41a of the connection portion 4 in the housing 51, it is substantially equivalent to increasing the surface area of the outer peripheral surface 41a of the connection portion 4 by an amount corresponding to the surface area of the plurality of heat sinks 54. Therefore, in the housing 51, the carrier gas CG contacts not only the outer peripheral surface 41a of the connection portion 4 but also the heat sinks 54 having a large surface area, so that the connection portion 4 can be efficiently radiated. That is, the cooling efficiency of the connection portion 4 can be improved.

以上所說明的液體材料汽化裝置1是汽化部3包括噴嘴N、連接部4包括連接管41、且冷卻部5冷卻連接部4(連接管41)的構造。在該構造中,藉由冷卻部5與載氣供給路21b連通,可將混合於液體材料LQ中的載氣CG有效地用作用以冷卻連接部4的氣體,抑制設置有液體材料汽化裝置1的半導體處理裝置的大型化及成本的增大等,可獲得上述本實施方式的效果。The liquid material vaporization device 1 described above is a structure in which the vaporization section 3 includes a nozzle N, the connection section 4 includes a connection tube 41, and the cooling section 5 cools the connection section 4 (connection tube 41). In this structure, the cooling section 5 is connected to the carrier gas supply path 21b, so that the carrier gas CG mixed in the liquid material LQ can be effectively used as a gas for cooling the connection section 4, and the size increase and cost increase of the semiconductor processing device provided with the liquid material vaporization device 1 can be suppressed, and the effect of the above-mentioned embodiment can be obtained.

〔4.液體材料汽化裝置的又一構造〕 圖6是示意性地表示本實施方式的液體材料汽化裝置1的又一構造的截面圖。圖6的液體材料汽化裝置1除了噴嘴N設置於作為汽化部3的外部的連接部4、冷卻部5冷卻亦包括噴嘴N在內的連接部4的方面以外,為與圖1同樣的構造。再者,圖3~圖5所示的冷卻部5的構造當然亦可應用於圖6的液體材料汽化裝置1。 [4. Another structure of the liquid material vaporization device] FIG. 6 is a cross-sectional view schematically showing another structure of the liquid material vaporization device 1 of the present embodiment. The liquid material vaporization device 1 of FIG. 6 has the same structure as FIG. 1 except that the nozzle N is provided in the connection part 4 which is the outside of the vaporization part 3 and the cooling part 5 cools the connection part 4 including the nozzle N. Furthermore, the structure of the cooling part 5 shown in FIG. 3 to FIG. 5 can of course also be applied to the liquid material vaporization device 1 of FIG. 6.

在圖6的液體材料汽化裝置1中,連接部4包括連接管41、及噴嘴N。噴嘴N位於連接管41與汽化部3之間,將氣液混合體MG噴霧至汽化部3的汽化室31內。即,噴嘴N位於汽化部3的外部、且汽化部3的上游側。冷卻部5的殼體51覆蓋連接管41及噴嘴N兩者。In the liquid material vaporization device 1 of FIG6 , the connection section 4 includes a connection tube 41 and a nozzle N. The nozzle N is located between the connection tube 41 and the vaporization section 3, and sprays the gas-liquid mixture MG into the vaporization chamber 31 of the vaporization section 3. That is, the nozzle N is located outside the vaporization section 3 and on the upstream side of the vaporization section 3. The housing 51 of the cooling section 5 covers both the connection tube 41 and the nozzle N.

即便為圖6的構造,亦與圖1的構造同樣,藉由冷卻部5與載氣供給路21b連通,可將混合於液體材料LQ中的載氣CG有效地用作用以冷卻連接部4的氣體,抑制設置有液體材料汽化裝置1的半導體處理裝置的大型化及成本的增大等,可獲得上述本實施方式的效果。Even in the structure of FIG. 6 , similar to the structure of FIG. 1 , by connecting the cooling section 5 with the carrier gas supply path 21 b, the carrier gas CG mixed in the liquid material LQ can be effectively used as a gas for cooling the connecting section 4, thereby suppressing the increase in size and cost of the semiconductor processing apparatus provided with the liquid material vaporization device 1, and achieving the effect of the above-mentioned present embodiment.

〔5.補充〕 在噴嘴N設置於汽化部3的外部(上游側)的構造中,連接部4可僅由噴嘴N構成。即,連接部4可為不包括連接管41而經由噴嘴N將流量控制閥2的氣液混合體排出路21c與汽化部3連接的構造。在該構造中,利用殼體51覆蓋噴嘴N的周圍,使載氣CG流至殼體51內,藉此將噴嘴N冷卻。因此,藉由使包括此種殼體51的冷卻部5與載氣供給路21b連通,可獲得與本實施方式同樣的效果。 [5. Supplement] In a structure where the nozzle N is arranged outside (upstream side) of the vaporization section 3, the connection section 4 may be composed only of the nozzle N. That is, the connection section 4 may be a structure that does not include the connection tube 41 and connects the gas-liquid mixture discharge path 21c of the flow control valve 2 to the vaporization section 3 via the nozzle N. In this structure, the nozzle N is covered with a shell 51, and the carrier gas CG flows into the shell 51, thereby cooling the nozzle N. Therefore, by connecting the cooling section 5 including such a shell 51 to the carrier gas supply path 21b, the same effect as the present embodiment can be obtained.

在本實施方式中,液體材料汽化裝置1所包括的流量控制閥2為常開型,但亦可將使載氣供給路21b與冷卻部5連通的本實施方式的構造應用於常閉型的流量控制閥2。在該情況下,氣液混合部29適當地變更為與常閉型相適應的構造即可。In the present embodiment, the flow control valve 2 included in the liquid material vaporization device 1 is a normally open type, but the structure of the present embodiment in which the carrier gas supply path 21b is connected to the cooling section 5 can also be applied to a normally closed type flow control valve 2. In this case, the gas-liquid mixing section 29 can be appropriately changed to a structure suitable for the normally closed type.

本實施方式的液體材料汽化裝置1在採用在流量控制閥2的內部將液體材料LQ與載氣CG混合而生成氣液混合體MG的內部混合方式的構造中,使載氣供給路21b與冷卻部5連通。與在流量控制閥2的外部將液體材料LQ與載氣CG混合的外部混合方式中,例如在向汽化室31內噴霧時,亦可使冷卻部5中冷卻噴嘴N後的載氣CG與液體材料LQ混合,在該情況下亦可獲得與本實施方式同樣的效果。The liquid material vaporizing device 1 of the present embodiment adopts an internal mixing method in which the liquid material LQ and the carrier gas CG are mixed inside the flow control valve 2 to generate a gas-liquid mixture MG, and the carrier gas supply path 21b is connected to the cooling section 5. In the external mixing method in which the liquid material LQ and the carrier gas CG are mixed outside the flow control valve 2, for example, when spraying into the vaporizing chamber 31, the carrier gas CG after the cooling nozzle N in the cooling section 5 can be mixed with the liquid material LQ, and in this case, the same effect as that of the present embodiment can be obtained.

以上,已對本發明的實施方式進行了說明,但本發明的範圍並不限定於此,可在不脫離發明的主旨的範圍內擴張或變更而實施。 [產業上的可利用性] The above has described the implementation method of the present invention, but the scope of the present invention is not limited thereto, and the present invention can be implemented by expansion or modification within the scope of the subject matter of the invention. [Industrial Applicability]

本發明可用於例如設置於半導體製造裝置的前段的汽化器。The present invention can be used, for example, in a vaporizer disposed at the front end of a semiconductor manufacturing device.

1:液體材料汽化裝置 2:流量控制閥 3:汽化部 4:連接部 5:冷卻部 21:本體區塊 21a:液體材料供給路 21b:載氣供給路 21c:氣液混合體排出路 21d:連通路 21S:閥座面 22:支持區塊 23:致動器 24:閥體 24S:落座面 25:隔膜 26:支持體 27:真球 28:柱塞 29:氣液混合部 29a:氣液混合室 31:汽化室 41:連接管 41a、51a:外周面 51:殼體 51P:氣體流路 52:導入口 53:導出口 54:散熱片 231:壓電堆 232:收容體 CG:載氣 FP:流路部 LQ:液體材料 MG:氣液混合體 N:噴嘴 T:切線 1: Liquid material vaporization device 2: Flow control valve 3: Vaporization section 4: Connection section 5: Cooling section 21: Main body block 21a: Liquid material supply path 21b: Carrier gas supply path 21c: Gas-liquid mixture discharge path 21d: Connection path 21S: Valve seat surface 22: Support block 23: Actuator 24: Valve body 24S: Seating surface 25: Diaphragm 26: Support body 27: True ball 28: Plunger 29: Gas-liquid mixing section 29a: Gas-liquid mixing chamber 31: Vaporization chamber 41: Connection tube 41a, 51a: Outer peripheral surface 51: Shell 51P: Gas flow path 52: Inlet 53: outlet 54: heat sink 231: piezoelectric stack 232: container CG: carrier gas FP: flow path LQ: liquid material MG: gas-liquid mixture N: nozzle T: tangent

圖1是示意性地表示本發明的一實施方式的液體材料汽化裝置的概略構造的截面圖。 圖2是表示使用所述液體材料汽化裝置使液體材料汽化的液體材料汽化方法的各步驟的流程的流程圖。 圖3是以與連接部中的氣液混合體的流動方向垂直的截面切斷所述液體材料汽化裝置所包括的冷卻部時的截面圖。 圖4是示意性地表示所述液體材料汽化裝置的另一構造的截面圖。 圖5是示意性地表示所述液體材料汽化裝置的又一構造的截面圖。 圖6是示意性地表示所述液體材料汽化裝置的又一構造的截面圖。 FIG. 1 is a cross-sectional view schematically showing the schematic structure of a liquid material vaporization device according to an embodiment of the present invention. FIG. 2 is a flow chart showing the flow of each step of a liquid material vaporization method for vaporizing a liquid material using the liquid material vaporization device. FIG. 3 is a cross-sectional view of a cooling portion included in the liquid material vaporization device when it is cut at a cross section perpendicular to the flow direction of the gas-liquid mixture in the connection portion. FIG. 4 is a cross-sectional view schematically showing another structure of the liquid material vaporization device. FIG. 5 is a cross-sectional view schematically showing another structure of the liquid material vaporization device. FIG. 6 is a cross-sectional view schematically showing another structure of the liquid material vaporization device.

1:液體材料汽化裝置 1: Liquid material vaporization device

2:流量控制閥 2: Flow control valve

3:汽化部 3: Vaporization section

4:連接部 4: Connection part

5:冷卻部 5: Cooling section

21:本體區塊 21: Body block

21a:液體材料供給路 21a: Liquid material supply line

21b:載氣供給路 21b: Carrier gas supply path

21c:氣液混合體排出路 21c: Gas-liquid mixture discharge path

21d:連通路 21d: Connecting passages

21S:閥座面 21S: Valve seat surface

22:支持區塊 22: Support block

23:致動器 23: Actuator

24:閥體 24: Valve body

24S:落座面 24S: Seating surface

25:隔膜 25: Diaphragm

26:支持體 26: Support body

27:真球 27: True Ball

28:柱塞 28: Plunger

29:氣液混合部 29: Gas-liquid mixing section

29a:氣液混合室 29a: Gas-liquid mixing chamber

31:汽化室 31: Vaporization chamber

41:連接管 41: Connecting pipe

51:殼體 51: Shell

52:導入口 52: Entryway

53:導出口 53: Export

231:壓電堆 231: Piezoelectric stack

232:收容體 232: Containment Body

CG:載氣 CG:Carrier gas

FP:流路部 FP: Flow path

LQ:液體材料 LQ: Liquid material

MG:氣液混合體 MG: gas-liquid mixture

N:噴嘴 N: Nozzle

Claims (11)

一種液體材料汽化裝置,包括: 氣液混合部,將液體材料與載氣混合而生成氣液混合體; 載氣供給路,向所述氣液混合部供給所述載氣; 流路部,供所述氣液混合部中所生成的所述氣液混合體流通; 汽化部,將在所述流路部中流通的所述氣液混合體所包含的所述液體材料加熱而使其汽化;及 冷卻部,將所述流路部冷卻, 所述冷卻部與所述載氣供給路連通。 A liquid material vaporization device comprises: a gas-liquid mixing section for mixing a liquid material with a carrier gas to generate a gas-liquid mixture; a carrier gas supply path for supplying the carrier gas to the gas-liquid mixing section; a flow path for circulating the gas-liquid mixture generated in the gas-liquid mixing section; a vaporization section for heating the liquid material contained in the gas-liquid mixture circulating in the flow path to vaporize it; and a cooling section for cooling the flow path, the cooling section being connected to the carrier gas supply path. 如請求項1所述的液體材料汽化裝置,其中所述流路部包括: 氣液混合體排出路,將所述氣液混合部中所生成的所述氣液混合體排出;及 連接部,將所述氣液混合體排出路與所述汽化部連接, 所述冷卻部將所述連接部冷卻。 The liquid material vaporization device as described in claim 1, wherein the flow path section includes: a gas-liquid mixture discharge path for discharging the gas-liquid mixture generated in the gas-liquid mixing section; and a connecting section for connecting the gas-liquid mixture discharge path to the vaporization section, and the cooling section for cooling the connecting section. 如請求項2所述的液體材料汽化裝置,其中所述冷卻部包括覆蓋所述連接部的周圍的殼體, 所述殼體與所述載氣供給路連通。 The liquid material vaporization device as described in claim 2, wherein the cooling portion includes a shell covering the periphery of the connecting portion, and the shell is connected to the carrier gas supply path. 如請求項3所述的液體材料汽化裝置,其中所述冷卻部包括: 導入口,向所述殼體內導入所述載氣;及 導出口,自所述殼體導出所述載氣, 所述載氣供給路與所述導出口連接。 The liquid material vaporization device as described in claim 3, wherein the cooling section includes: an inlet for introducing the carrier gas into the housing; and an outlet for conducting the carrier gas out of the housing, and the carrier gas supply path is connected to the outlet. 如請求項4所述的液體材料汽化裝置,其中所述導入口相對於所述導出口而位於所述汽化部的側。A liquid material vaporization device as described in claim 4, wherein the inlet is located on the side of the vaporization portion relative to the outlet. 如請求項4所述的液體材料汽化裝置,其中在與所述連接部中的所述氣液混合體的流動方向垂直的截面內, 所述導入口位於與針對所述殼體的外周面的切線重合的位置。 The liquid material vaporization device as described in claim 4, wherein in a cross section perpendicular to the flow direction of the gas-liquid mixture in the connecting portion, the inlet is located at a position that coincides with a tangent to the outer peripheral surface of the shell. 如請求項3所述的液體材料汽化裝置,其中所述殼體包括氣體流路,所述氣體流路以螺旋狀形成於所述連接部的周圍。A liquid material vaporization device as described in claim 3, wherein the shell includes a gas flow path, and the gas flow path is formed in a spiral shape around the connecting portion. 如請求項2所述的液體材料汽化裝置,其中所述冷卻部包括散熱片,所述散熱片與所述連接部的外周面連結。A liquid material vaporization device as described in claim 2, wherein the cooling part includes a heat sink connected to the outer peripheral surface of the connecting part. 如請求項2所述的液體材料汽化裝置,其中所述汽化部包括噴嘴,所述噴嘴將所述氣液混合體噴霧至汽化室內, 所述連接部包括連接管,所述連接管將所述氣液混合體排出路與所述噴嘴連接。 The liquid material vaporization device as described in claim 2, wherein the vaporization section includes a nozzle, and the nozzle sprays the gas-liquid mixture into the vaporization chamber, and the connecting section includes a connecting tube, and the connecting tube connects the gas-liquid mixture discharge path to the nozzle. 如請求項2所述的液體材料汽化裝置,其中所述連接部包括: 連接管,與所述氣液混合體排出路連接;及 噴嘴,位於所述連接管與所述汽化部之間,將所述氣液混合體噴霧至所述汽化部的汽化室內。 The liquid material vaporization device as described in claim 2, wherein the connection portion includes: a connection pipe connected to the gas-liquid mixture discharge path; and a nozzle located between the connection pipe and the vaporization portion to spray the gas-liquid mixture into the vaporization chamber of the vaporization portion. 一種液體材料汽化方法,包括: 氣液混合體生成步驟,在氣液混合部中將液體材料與載氣混合,藉此生成氣液混合體; 汽化步驟,將所述氣液混合部中所生成並經由流路部供給至汽化部的所述氣液混合體所包含的所述液體材料在所述汽化部中加熱而使其汽化; 冷卻步驟,藉由所述載氣的供給將所述流路部冷卻;及 載氣供給步驟,將所述冷卻步驟中冷卻所述流路部後的所述載氣經由載氣供給路供給至所述氣液混合部。 A method for vaporizing a liquid material comprises: a gas-liquid mixture generating step, mixing a liquid material with a carrier gas in a gas-liquid mixing section to generate a gas-liquid mixture; a vaporizing step, heating the liquid material contained in the gas-liquid mixture generated in the gas-liquid mixing section and supplied to the vaporizing section via a flow path section in the vaporizing section to vaporize the liquid material; a cooling step, cooling the flow path section by supplying the carrier gas; and a carrier gas supplying step, supplying the carrier gas after cooling the flow path section in the cooling step to the gas-liquid mixing section via a carrier gas supply path.
TW112138267A 2022-10-12 2023-10-05 Liquid material vaporizer and liquid material vaporization method TW202419676A (en)

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