JP2020169737A - Gas-phase type heating apparatus - Google Patents

Gas-phase type heating apparatus Download PDF

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JP2020169737A
JP2020169737A JP2019069897A JP2019069897A JP2020169737A JP 2020169737 A JP2020169737 A JP 2020169737A JP 2019069897 A JP2019069897 A JP 2019069897A JP 2019069897 A JP2019069897 A JP 2019069897A JP 2020169737 A JP2020169737 A JP 2020169737A
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智大 宇治野
Tomohiro Ujino
智大 宇治野
永井 耕一
Koichi Nagai
耕一 永井
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Panasonic Intellectual Property Management Co Ltd
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Abstract

To provide a gas-phase type heating apparatus that supplies vapor instantaneously into a vapor heating furnace utilizing pressure reduction in the vapor heating furnace, the pressure reduction being caused by heating a to-be-heated article.SOLUTION: A gas-phase type heating apparatus of this invention is provided with a space in a side part of the vapor heating furnace 101 where vapor is stored and a mechanism that varies a volume of the space where the vapor is stored so as to maintain a pressure in the furnace constant by making up for a pressure change due to vapor reduction when a vapor amount is reduced by heating a to-be-heated article 102, thereby vapor is instantaneously supplied to the vicinity of the to-be-heated article from the space where the vapor is stored, the space being provided in the side part of the vapor heating furnace.SELECTED DRAWING: Figure 2

Description

本発明は、熱転移液の蒸気の凝縮潜熱を利用して、被加熱物を加熱する気相式加熱装置に関するものである。 The present invention relates to a vapor phase heating device that heats an object to be heated by utilizing the latent heat of condensation of the vapor of the thermal transfer liquid.

近年、様々な工業製品もしくは家電の組み立て製造工程、又はそれらの製品の構成部品となる各種電子部品、各種の電池、もしくは、電子部品が実装された基板などのデバイス製造工程において、各種熱処理装置で処理される被加熱物の形状が複雑化している。例えば、電子部品が実装された基板においても、平面基板だけでなく、立体的な基板の水平面以外の部分に、はんだペーストを塗布してはんだペーストの上に電子部品を配置しただけの電子部品の保持力が弱い状態で、はんだペーストを溶融して接合するための加熱処理が行われている。また、立体となることで、被加熱物の熱容量そのものも、増加する傾向にある。ここで、各種熱処理装置とは、例えば乾燥炉、キュア炉、もしくは電子部品の実装工程などではんだ付けに使用されるリフロー炉などである。 In recent years, in various heat treatment devices in the assembly manufacturing process of various industrial products or home appliances, or in the device manufacturing process of various electronic parts, various batteries, or substrates on which electronic parts are mounted, which are constituent parts of those products. The shape of the object to be treated is complicated. For example, even in a substrate on which electronic components are mounted, not only a flat substrate but also an electronic component in which solder paste is applied to a portion of a three-dimensional substrate other than the horizontal plane and the electronic components are arranged on the solder paste. A heat treatment is performed to melt and join the solder paste in a state where the holding power is weak. In addition, the heat capacity of the object to be heated tends to increase due to the three-dimensional shape. Here, the various heat treatment devices are, for example, a drying furnace, a curing furnace, a reflowing furnace used for soldering in a mounting process of electronic components, and the like.

これらの被加熱物の加熱工程では、不均一な加熱能力による被加熱物の各箇所における温度上昇のばらつきがある場合は、加熱工程の所望の所要時間を得るために、全ての部分が、所望の温度に昇温した状態から、さらに所望の時間を保持する必要がある。また、昇温の遅い部分を所望の時間だけ保持するためには、昇温の早い部分は、必要以上の熱にさらされることになる。また、被加熱物において特に熱影響の大きい場合は、品質への影響が懸念される。また、熱風の衝突による熱伝達を利用した加熱工程の場合、被加熱物の熱容量が大きい場合は、所望の昇温速度を得るために、熱風の被加熱物への衝突速度を速めることで、熱伝達率を高くすることが出来る。しかしながら、例えば、立体的な基板の水平面以外の部分に、はんだペーストを塗布して電子部品を配置しただけの保持力が弱い状態で加熱処理をする必要がある場合、はんだの溶融、その後の冷却によるはんだの凝固が完了する以前に、熱風を高速で衝突させることで、部品が基板から剥離してしまう可能性が大きくなる。 In these heating steps of the object to be heated, if there are variations in temperature rise at each location of the object to be heated due to non-uniform heating capacity, all parts are desired in order to obtain the desired time required for the heating step. It is necessary to keep the desired time from the state where the temperature has been raised to the above temperature. Further, in order to hold the portion where the temperature rise is slow for a desired time, the portion where the temperature rises quickly is exposed to more heat than necessary. Further, when the object to be heated has a particularly large thermal effect, there is a concern that the quality may be affected. Further, in the case of a heating process using heat transfer due to collision of hot air, when the heat capacity of the object to be heated is large, the collision rate of hot air with the object to be heated is increased in order to obtain a desired rate of temperature rise. The heat transfer coefficient can be increased. However, for example, when it is necessary to apply a solder paste to a portion of a three-dimensional substrate other than the horizontal plane and heat-treat the electronic components in a state where the holding force is weak, the solder is melted and then cooled. By colliding hot air at high speed before the solidification of the solder is completed, there is a high possibility that the components will peel off from the substrate.

そこで、熱容量の大きい基板についても熱風の衝突による部品の剥離などを回避し、高い熱伝達率を利用して被加熱物を効率良く加熱する方法として、熱転移液の蒸気が有する凝縮潜熱を利用して加熱する気相式加熱装置が知られている(例えば、特許文献1参照)。 Therefore, as a method of efficiently heating the object to be heated by avoiding peeling of parts due to collision of hot air even for a substrate having a large heat capacity and utilizing a high heat transfer coefficient, the latent heat of condensation contained in the vapor of the heat transfer liquid is used. A vapor phase heating device is known for heating (see, for example, Patent Document 1).

図7は特許文献1の概略構成図である。特許文献1で開示されている構成は、以下のような構成である。加熱装置10は、搬入口8と、搬出口9と、コンベア3と、ヒータ4、温度センサ6、電力調節器11を備えた蒸気槽1とで構成されている。搬入口8から投入された被加熱物2は、コンベア3によって蒸気槽1まで搬送され、蒸気槽1内で加熱された後、コンベア3によって搬出口9まで搬送され、加熱装置10外へ搬出される。蒸気槽1内の底部には、対空気比重の大きい熱転移液5が保持されており、蒸気槽1内の底部に設置されたヒータ4で熱転移液5を加熱し、蒸気7を発生させている。蒸気槽1の上部には温度センサ6が設置されており、蒸気槽1の底部で発生した蒸気7が押し上げられ、蒸気7と空気との境界面である蒸気面が温度センサ6の先端6aの高さに到達すると、温度センサ6の先端6aが蒸気7の温度を検知するため、電力調節器11によってヒータ4の出力を制御することで、蒸気面を温度センサ6の先端6aの高さに維持するように調節することができる。温度センサ6の先端6aは、高さ方向に上下移動できるようになっており、被加熱物2がコンベア3上に無い場合は、温度センサ6の先端6aの高さを低く設定し、蒸気7の発生量を抑制する。そして、被加熱物2がコンベア3上にある場合は、温度センサ6の先端6aの高さを高く設定し、蒸気槽1内の蒸気量を増やし、その蒸気7の凝縮潜熱によって被加熱物2を加熱する。 FIG. 7 is a schematic configuration diagram of Patent Document 1. The configuration disclosed in Patent Document 1 is as follows. The heating device 10 includes a carry-in inlet 8, a carry-out port 9, a conveyor 3, a heater 4, a temperature sensor 6, and a steam tank 1 provided with a power controller 11. The object to be heated 2 introduced from the carry-in inlet 8 is conveyed to the steam tank 1 by the conveyor 3, heated in the steam tank 1, then conveyed to the carry-out port 9 by the conveyor 3, and carried out of the heating device 10. Ru. A heat transfer liquid 5 having a large specific gravity to air is held at the bottom of the steam tank 1, and a heater 4 installed at the bottom of the steam tank 1 heats the heat transfer liquid 5 to generate steam 7. ing. A temperature sensor 6 is installed in the upper part of the steam tank 1, the steam 7 generated at the bottom of the steam tank 1 is pushed up, and the steam surface which is the interface between the steam 7 and the air is the tip 6a of the temperature sensor 6. When the height is reached, the tip 6a of the temperature sensor 6 detects the temperature of the steam 7, so that the output of the heater 4 is controlled by the power regulator 11 to raise the steam surface to the height of the tip 6a of the temperature sensor 6. It can be adjusted to maintain. The tip 6a of the temperature sensor 6 can move up and down in the height direction, and when the object to be heated 2 is not on the conveyor 3, the height of the tip 6a of the temperature sensor 6 is set low and the steam 7 Suppress the amount of When the object 2 to be heated is on the conveyor 3, the height of the tip 6a of the temperature sensor 6 is set high, the amount of steam in the steam tank 1 is increased, and the latent heat of condensation of the steam 7 causes the object 2 to be heated 2 to be heated. To heat.

特開平5-111755号公報Japanese Patent Application Laid-Open No. 5-111755

しかしながら、前記特許文献1の構成では、被加熱物の加熱により蒸気槽内の蒸気量が減少したときに、温度センサで蒸気面の低下を検知してからヒータの出力を上げ、熱転移液を加熱するように構成している。このため、被加熱物近傍への蒸気の供給には、蒸気槽の底部から被加熱物が位置する高さまで熱転移液の蒸気が上昇するまでの時間を要し、被加熱物の加熱による蒸気の減少と被加熱物近傍への蒸気の供給に時間差が生じるため、プロセス時間が長くなるという課題がある。 However, in the configuration of Patent Document 1, when the amount of steam in the steam tank decreases due to the heating of the object to be heated, the temperature sensor detects the decrease in the steam level and then the output of the heater is increased to generate the heat transfer liquid. It is configured to heat. Therefore, in order to supply steam to the vicinity of the object to be heated, it takes time for the steam of the thermal transfer liquid to rise from the bottom of the steam tank to the height at which the object to be heated is located, and the steam generated by heating the object to be heated. There is a problem that the process time becomes long because there is a time lag between the decrease in the amount of steam and the supply of steam to the vicinity of the object to be heated.

本発明は、このような点を鑑み、被加熱物の加熱によって蒸気量が減少した際に、被加熱物近傍に蒸気を即時に供給する、気相式加熱装置を提供することを目的とする。 In view of these points, an object of the present invention is to provide a vapor-phase heating device that immediately supplies steam to the vicinity of the object to be heated when the amount of steam decreases due to heating of the object to be heated. ..

前記目的を達成するために、本発明の1つの態様にかかる気相式加熱装置は、
熱転移液の蒸気の凝縮潜熱を利用して被加熱物を加熱する気相式加熱装置であって、
外部空間から内部空間が遮断される蒸気加熱炉と、
前記蒸気加熱炉に前記蒸気を供給する蒸気供給部と、
前記蒸気加熱炉で加熱位置と搬送位置との間で前記被加熱物を搬送する搬送部と、
前記蒸気加熱炉で、前記加熱位置の前記被加熱物の上端より上方に設けられた冷却部と、
前記蒸気加熱炉の側部に設けられて前記蒸気加熱炉と接続口を介して連通可能に前記蒸気を蓄える蒸気保持部とを有し、
前記蒸気保持部は、
前記蒸気加熱炉に連通する第1の空間と、
内部空間の容積が変化することにより前記第1の空間の容積を変化させる第2の空間と、
前記第1の空間と前記第2の空間とを仕切る仕切り部とを有し、
前記蒸気保持部と前記蒸気加熱炉とを接続する前記接続口の下端の高さは、前記被加熱物の前記加熱位置の前記被加熱物の下端より上方に配置され、前記接続口の上端の高さは、前記冷却部より下方で、且つ前記被加熱物の前記加熱位置の前記被加熱物の上端より上方に配置され、
前記蒸気加熱炉内の前記冷却部より下方の空間が前記蒸気で満たされているときは、前記仕切り部の移動により前記第2の空間の容積が減少し、前記第1の空間に前記蒸気が取り込まれ、前記蒸気加熱炉内の前記蒸気が減少したときは、前記第1の空間と前記第2の空間との間の圧力差に基づく前記仕切り部の移動により、前記第2の空間の容積が増加し、前記第1の空間に取り込まれた前記蒸気を前記蒸気加熱炉内に供給する。
In order to achieve the above object, the gas phase heating device according to one aspect of the present invention is
It is a vapor phase heating device that heats the object to be heated by utilizing the latent heat of condensation of the vapor of the thermal transfer liquid.
A steam heating furnace that cuts off the internal space from the external space,
A steam supply unit that supplies the steam to the steam heating furnace,
A transport unit that transports the object to be heated between the heating position and the transport position in the steam heating furnace, and
In the steam heating furnace, a cooling unit provided above the upper end of the object to be heated at the heating position and
It has a steam heating furnace provided on a side portion of the steam heating furnace and a steam holding portion for storing the steam so as to be able to communicate with each other through a connection port.
The steam holding part is
The first space communicating with the steam heating furnace and
A second space that changes the volume of the first space by changing the volume of the internal space, and
It has a partition portion that separates the first space from the second space.
The height of the lower end of the connection port connecting the steam holding portion and the steam heating furnace is arranged above the lower end of the heated object at the heating position of the heated object, and is located at the upper end of the connecting port. The height is arranged below the cooling unit and above the upper end of the heated object at the heating position of the heated object.
When the space below the cooling portion in the steam heating furnace is filled with the steam, the volume of the second space is reduced by the movement of the partition portion, and the steam is filled in the first space. When the steam is taken in and the steam in the steam heating furnace is reduced, the volume of the second space is increased by the movement of the partition portion based on the pressure difference between the first space and the second space. Increases, and the steam taken into the first space is supplied into the steam heating furnace.

以上のように、本発明の前記態様の気相式加熱装置によれば、被加熱物の加熱により蒸気加熱炉内の蒸気量が減少した際に、蒸気を被加熱物近傍に即時に供給することができ、プロセス時間を短縮することが可能となる。 As described above, according to the vapor phase heating apparatus of the above aspect of the present invention, when the amount of steam in the steam heating furnace is reduced due to the heating of the object to be heated, the steam is immediately supplied to the vicinity of the object to be heated. It is possible to shorten the process time.

本発明の実施形態における気相式加熱装置の側面から見た概略構成図Schematic configuration diagram seen from the side of the gas phase heating device according to the embodiment of the present invention. 本発明の実施形態における気相式加熱装置の正面から見た概略構成図Schematic configuration diagram seen from the front of the vapor phase heating apparatus according to the embodiment of the present invention. 本発明の実施形態における気相式加熱装置の正面から見た概略構成図Schematic configuration diagram seen from the front of the vapor phase heating apparatus according to the embodiment of the present invention. 本発明の実施形態における気相式加熱装置の説明図Explanatory drawing of vapor-phase heating apparatus in embodiment of this invention 本発明の実施形態における気相式加熱装置の説明図Explanatory drawing of vapor-phase heating apparatus in embodiment of this invention 本発明の実施形態における気相式加熱装置の説明図Explanatory drawing of vapor-phase heating apparatus in embodiment of this invention 従来の気相式加熱装置の概略構成図Schematic configuration of a conventional gas phase heating device

以下、本発明の実施の形態について、図面を参照しながら説明する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings.

図1は、本発明の実施形態における気相式加熱装置100の側面から見た概略構成図である。 FIG. 1 is a schematic configuration diagram viewed from the side of the gas phase heating device 100 according to the embodiment of the present invention.

気相式加熱装置100は、熱転移液106の蒸気の凝縮潜熱を利用して被加熱物102を加熱する装置であり、少なくとも、蒸気加熱炉101と、蒸気供給部107と、搬送部103Bと、冷却部110と、蒸気保持部111とを有している。 The vapor phase heating device 100 is a device that heats the object to be heated 102 by utilizing the latent heat of condensation of the steam of the heat transfer liquid 106, and at least the steam heating furnace 101, the steam supply unit 107, and the transport unit 103B. , A cooling unit 110 and a steam holding unit 111.

蒸気加熱炉101は、外部空間90から内部空間101aが遮断されて、底部に熱転移液106が保持されているとともに、加熱処理時には、被加熱物102を内部で加熱する。 In the steam heating furnace 101, the internal space 101a is cut off from the external space 90, the heat transfer liquid 106 is held at the bottom, and the object to be heated 102 is heated internally during the heat treatment.

蒸気供給部107は、蒸気加熱炉101の底部に配置されて、熱転移液106を加熱して、蒸気加熱炉101内に熱転移液106の蒸気108を供給する。 The steam supply unit 107 is arranged at the bottom of the steam heating furnace 101 to heat the heat transfer liquid 106 and supply the steam 108 of the heat transfer liquid 106 into the steam heating furnace 101.

搬送部103Bは、蒸気加熱炉101内で被加熱物102を搬送位置と加熱位置との間で搬送する。 The transport unit 103B transports the object to be heated 102 between the transport position and the heating position in the steam heating furnace 101.

冷却部110は、蒸気加熱炉101で、加熱時言い換えれば加熱位置の被加熱物102の上端より上方に設けられている。 The cooling unit 110 is provided in the steam heating furnace 101, in other words, above the upper end of the object to be heated 102 at the heating position.

蒸気保持部111は、蒸気加熱炉101の側部に設けられて、蒸気加熱炉101と接続口92を介して連通可能に、熱転移液106の蒸気を蓄えている。 The steam holding portion 111 is provided on the side portion of the steam heating furnace 101, and stores the steam of the heat transfer liquid 106 so as to be able to communicate with the steam heating furnace 101 via the connection port 92.

気相式加熱装置100は、より具体的には、加熱準備室104と蒸気加熱炉101の上部とが連結している。開閉可能な第1シャッタ105Aによって、外部空間90と加熱準備室104とが仕切られている。また、開閉可能な第2シャッタ105Bによって、加熱準備室104と蒸気加熱炉101が仕切られている。 More specifically, in the vapor phase heating device 100, the heating preparation chamber 104 and the upper part of the steam heating furnace 101 are connected to each other. The external space 90 and the heating preparation chamber 104 are separated by a first shutter 105A that can be opened and closed. Further, the heating preparation chamber 104 and the steam heating furnace 101 are separated by a second shutter 105B that can be opened and closed.

被加熱物102を気相式加熱装置100内に投入するとき以外は、第1、第2シャッタ105A、105Bを閉じた状態になっている。加熱準備室104には、ポンプと開放弁と等で構成された圧力調節部117が接続されており、加熱準備室104内の圧力を任意の値に圧力調節部117で調節できるようになっている。 The first and second shutters 105A and 105B are in the closed state except when the object to be heated 102 is put into the vapor phase heating device 100. A pressure adjusting unit 117 composed of a pump, an release valve, etc. is connected to the heating preparation chamber 104, and the pressure in the heating preparation chamber 104 can be adjusted to an arbitrary value by the pressure adjusting unit 117. There is.

加熱準備室104と蒸気加熱炉101とには、それぞれ圧力計119A、119Bが設置されて、加熱準備室104内の圧力と蒸気加熱炉101内の圧力とをそれぞれ計測している。計測されたそれら二つの圧力計119A、119Bの値を基に、圧力調節部117を制御する圧力制御部118が設置されている。 Pressure gauges 119A and 119B are installed in the heating preparation chamber 104 and the steam heating furnace 101, respectively, to measure the pressure in the heating preparation chamber 104 and the pressure in the steam heating furnace 101, respectively. A pressure control unit 118 that controls the pressure adjustment unit 117 is installed based on the measured values of the two pressure gauges 119A and 119B.

被加熱物102を蒸気加熱炉101内に投入する際には、まず、第1シャッタ105Aを開け、加熱準備室104内の第1搬送ステージ103A上に被加熱物102を搬入する。次いで、第1シャッタ105Aを閉じた後、圧力調節部117によって加熱準備室104内の圧力を蒸気加熱炉101内と同等の圧力に調節する。その後、第2シャッタ105Bを開け、被加熱物102を蒸気加熱炉101内の搬送位置の第2搬送ステージ103B上に搬送し、第2シャッタ105Bを閉じる。第2搬送ステージ103Bは搬送部の一例として機能する。第2搬送ステージ103Bは、被加熱物102を載置した状態で、上側の搬送位置と下側の加熱位置との間で蒸気加熱炉101内で昇降可能としている。すなわち、第2搬送ステージ103Bは、被加熱物102を載置した状態で、搬送位置から、後述するように蒸気加熱炉101内の冷却部110より下方でかつ蒸気108で満たされている空間内の加熱位置まで、被加熱物102を下降可能とする。 When the object to be heated 102 is put into the steam heating furnace 101, first, the first shutter 105A is opened, and the object to be heated 102 is carried onto the first transfer stage 103A in the heating preparation chamber 104. Next, after closing the first shutter 105A, the pressure in the heating preparation chamber 104 is adjusted to the same pressure as in the steam heating furnace 101 by the pressure adjusting unit 117. After that, the second shutter 105B is opened, the object to be heated 102 is conveyed onto the second transfer stage 103B at the transfer position in the steam heating furnace 101, and the second shutter 105B is closed. The second transfer stage 103B functions as an example of the transfer unit. The second transfer stage 103B can move up and down in the steam heating furnace 101 between the upper transfer position and the lower heating position in a state where the object to be heated 102 is placed. That is, the second transport stage 103B is in a space in which the object to be heated 102 is placed, below the cooling portion 110 in the steam heating furnace 101 and filled with steam 108, as will be described later. The object to be heated 102 can be lowered to the heating position of.

一方、被加熱物102を蒸気加熱炉101から取り出す際は、加熱準備室104内の圧力を蒸気加熱炉101内と同等の圧力に圧力調節部117で調節した後、第2シャッタ105Bを開け、被加熱物102を、搬送位置の第2搬送ステージ103Bから第1搬送ステージ103Aに搬送し、第2シャッタ105Bを閉じる。その後、圧力調節部117で加熱準備室104内の圧力を外部空間90の大気圧と同等の圧力に調節し、第1シャッタ105Aを開け、被加熱物102を気相式加熱装置外の外部空間90に取り出す。 On the other hand, when the object to be heated 102 is taken out from the steam heating furnace 101, the pressure in the heating preparation chamber 104 is adjusted to the same pressure as in the steam heating furnace 101 by the pressure adjusting unit 117, and then the second shutter 105B is opened. The object to be heated 102 is transported from the second transport stage 103B at the transport position to the first transport stage 103A, and the second shutter 105B is closed. After that, the pressure adjusting unit 117 adjusts the pressure inside the heating preparation chamber 104 to a pressure equivalent to the atmospheric pressure of the external space 90, opens the first shutter 105A, and moves the object to be heated 102 to the external space outside the gas phase heating device. Take out to 90.

また、蒸気加熱炉101は、詳しくは後述するが、ヒータ107と冷却コイル110とを備えており、ヒータ107で熱転移液106を加熱し、蒸気108を発生させている。冷却コイル110は冷却部の一例として機能する。ヒータ107は蒸気供給部の一例として機能する。 Further, as will be described in detail later, the steam heating furnace 101 includes a heater 107 and a cooling coil 110, and the heater 107 heats the heat transfer liquid 106 to generate steam 108. The cooling coil 110 functions as an example of the cooling unit. The heater 107 functions as an example of a steam supply unit.

図2及び図3は、本発明の第1実施形態における気相式加熱装置100の正面から見た概略構成図である。図2のように、気相式加熱装置100の蒸気加熱炉101の底部には、所定量の熱転移液106が保持されており、その熱転移液106を加熱し、蒸気108にするヒータ107が備わっている。蒸気加熱炉101の上方の壁面には、配管内に冷却水を循環させる冷却コイル110が備わっている。蒸気加熱炉101の底部で蒸発し、蒸気加熱炉101の内部空間101a内を上昇する蒸気108が冷却コイル110の高さに達すると、蒸気108が冷却コイル110で冷やされて凝縮し、熱転移液106に戻り、蒸気加熱炉101内の壁面を伝って、底部の熱転移液106に再び供給される。この冷却コイル110により、内部空間101a内で熱転移液106の蒸気108と空気との境界面である蒸気面109の高さが、冷却コイル110の高さに設定される。 2 and 3 are schematic configuration views of the gas phase heating device 100 according to the first embodiment of the present invention as viewed from the front. As shown in FIG. 2, a predetermined amount of the heat transfer liquid 106 is held at the bottom of the steam heating furnace 101 of the vapor phase heating device 100, and the heater 107 that heats the heat transfer liquid 106 to make steam 108. Is equipped. On the wall surface above the steam heating furnace 101, a cooling coil 110 for circulating cooling water in the piping is provided. When the steam 108 that evaporates at the bottom of the steam heating furnace 101 and rises in the internal space 101a of the steam heating furnace 101 reaches the height of the cooling coil 110, the steam 108 is cooled by the cooling coil 110, condensed, and heat-transferred. It returns to the liquid 106, travels along the wall surface in the steam heating furnace 101, and is supplied again to the heat transfer liquid 106 at the bottom. The cooling coil 110 sets the height of the steam surface 109, which is the interface between the steam 108 of the heat transfer liquid 106 and the air, to the height of the cooling coil 110 in the internal space 101a.

また、蒸気加熱炉101の側部には、冷却コイル110の高さよりも低い位置で内部空間101aと接続口92を介して連通する蒸気保持部111が設置されている。蒸気保持部111は、内部の空間を上下に2分割するように、蒸気保持部111内を摺動可能な仕切り部112によって仕切られて、第1の空間(例えば図2では上側の空間)113と第2の空間(例えば図2では下側の空間)114とが形成されている。仕切り部112によって仕切られた蒸気保持部111内の第1の空間113は、蒸気加熱炉101の内部空間101aに連通するように接続されている。一方、仕切り部112によって仕切られた蒸気保持部111内の第2の空間114は、外部空間90から遮断された密閉構造になっており、第2の空間114内の圧力を調節できるように圧力調節接続部116を有している。圧力調節接続部116は、弁を有しており、第2の空間114の圧力を調節するときは、弁を開放して第2の空間114と外部空間90とを連通させ、ポンプなどの圧力調節器を圧力調節接続部116に接続し、第2の空間114を所望の圧力に調節する。それ以外のときは、圧力調節接続部116の弁を閉じて第2の空間114を外部空間90から遮断するようにしている。仕切り部112は、第1の空間113と第2の空間114との圧力差に応じて自在に上下に移動可能となっている。よって、第2の空間114の内部空間の容積が変化することにより、第1の空間113の容積を変化させるようになっている。また、蒸気保持部111内には、仕切り部112がある一定の高さ以上にならないように保持する固定部115を有している。 Further, on the side portion of the steam heating furnace 101, a steam holding portion 111 that communicates with the internal space 101a via the connection port 92 is installed at a position lower than the height of the cooling coil 110. The steam holding portion 111 is partitioned by a slidable partition portion 112 in the steam holding portion 111 so as to divide the internal space into upper and lower parts, and the first space (for example, the upper space in FIG. 2) 113 And a second space (for example, the lower space in FIG. 2) 114 are formed. The first space 113 in the steam holding portion 111 partitioned by the partition portion 112 is connected so as to communicate with the internal space 101a of the steam heating furnace 101. On the other hand, the second space 114 in the steam holding portion 111 partitioned by the partition portion 112 has a closed structure shielded from the external space 90, and the pressure in the second space 114 can be adjusted. It has an adjustment connection 116. The pressure adjusting connection portion 116 has a valve, and when adjusting the pressure in the second space 114, the valve is opened to allow the second space 114 and the external space 90 to communicate with each other, and the pressure of a pump or the like is adjusted. A regulator is connected to the pressure control connection 116 to adjust the second space 114 to the desired pressure. At other times, the valve of the pressure adjusting connection 116 is closed to shut off the second space 114 from the external space 90. The partition portion 112 can freely move up and down according to the pressure difference between the first space 113 and the second space 114. Therefore, the volume of the first space 113 is changed by changing the volume of the internal space of the second space 114. Further, the steam holding portion 111 has a fixing portion 115 that holds the partition portion 112 so as not to exceed a certain height.

気相式加熱装置100の運転開始前の初期状態においては、第2の空間114内の圧力は、仕切り部112に掛かる重力による下方向の力を少し上回り、仕切り部112が固定部115の高さまで押し上げられ、固定部115に接触した状態になる程度に、大気圧に対して正圧に設定されている。 In the initial state before the start of operation of the gas phase heating device 100, the pressure in the second space 114 slightly exceeds the downward force due to the gravity applied to the partition portion 112, and the partition portion 112 is the height of the fixed portion 115. The pressure is set to positive with respect to the atmospheric pressure to the extent that it is pushed up to the extent that it comes into contact with the fixed portion 115.

気相式加熱装置100の運転が開始されると、まず、蒸気加熱炉101内でヒータ107により熱転移液106が加熱され、熱転移液106は、蒸発して蒸気108になり、蒸気加熱炉101内の冷却コイル110より下方の空間を満たしていく。一定時間が経過すると、蒸気加熱炉101内の冷却コイル110より下方の空間は、熱転移液106の沸点の温度の蒸気108で満たされるようになり、前述したように、蒸気面109は、冷却コイル110の高さに維持される。 When the operation of the vapor phase heating device 100 is started, first, the heat transfer liquid 106 is heated by the heater 107 in the steam heating furnace 101, and the heat transfer liquid 106 evaporates to steam 108, and the steam heating furnace The space below the cooling coil 110 in 101 is filled. After a certain period of time, the space below the cooling coil 110 in the steam heating furnace 101 is filled with steam 108 having a boiling point temperature of the heat transfer liquid 106, and as described above, the steam surface 109 is cooled. It is maintained at the height of the coil 110.

それと同時に、蒸気108は、接続口92を介して、蒸気保持部111内の第1の空間113内にも拡散するため、第1の空間113内も蒸気108で満たされた状態になる。その状態になると、蒸気加熱炉101と第1の空間113内との圧力は、熱転移液106の沸点の蒸気圧分だけ上昇するため、蒸気保持部111内の仕切り部112は、第1の空間113の圧力に押されて、下方向に移動する。仕切り部112の下方向への移動により、第2の空間114の容積が減少するため、その容積の減少に反比例して、第2の空間114の圧力が上昇する。図3のように、第2の空間114内の圧力が蒸気加熱炉101内の圧力と釣り合ったところで、仕切り部112が停止し、第1の空間113は、第2の空間114の容積が減少した分だけ容積が増加し、その容積分の蒸気108が第1の空間113内に蓄えられる。 At the same time, the steam 108 diffuses into the first space 113 in the steam holding portion 111 through the connection port 92, so that the first space 113 is also filled with the steam 108. In that state, the pressure between the steam heating furnace 101 and the inside of the first space 113 increases by the vapor pressure at the boiling point of the heat transfer liquid 106, so that the partition portion 112 in the steam holding portion 111 is the first. Pushed by the pressure of space 113, it moves downward. Since the volume of the second space 114 decreases due to the downward movement of the partition portion 112, the pressure of the second space 114 increases in inverse proportion to the decrease in the volume. As shown in FIG. 3, when the pressure in the second space 114 is balanced with the pressure in the steam heating furnace 101, the partition portion 112 is stopped, and the volume of the second space 114 in the first space 113 is reduced. The volume is increased by that amount, and the steam 108 for that volume is stored in the first space 113.

次いで、図4及び図5は、蒸気加熱炉101内に導入した被加熱物102を蒸気108によって加熱するときの説明図である。被加熱物102を載せた第2搬送ステージ103Bを、蒸気加熱炉101内でかつ冷却コイル110より下方の蒸気108で満たされている空間まで下降させると、被加熱物102の周辺の蒸気108が被加熱物102の表面で凝縮し、凝縮潜熱によって被加熱物102が加熱される。さらに、蒸気108の凝縮による蒸気量の減少に伴い、被加熱物102の周辺の圧力が減少するため、蒸気加熱炉101内に圧力分布が生じる。すると、その圧力差によって、被加熱物102の上方に存在する蒸気108が、被加熱物102に接近する方向に引き寄せられ、蒸気面109の高さが下降する。また、蒸気加熱炉101内の蒸気108の凝縮が進むと、蒸気加熱炉101内全体の圧力が減少するため、蒸気保持部111内の仕切り部112が第2の空間114の圧力によって押され、仕切り部112が上方向へ移動する。 Next, FIGS. 4 and 5 are explanatory views when the object to be heated 102 introduced into the steam heating furnace 101 is heated by the steam 108. When the second transfer stage 103B on which the object to be heated 102 is placed is lowered to a space in the steam heating furnace 101 and below the cooling coil 110 and filled with steam 108, the steam 108 around the object to be heated 102 is generated. It condenses on the surface of the object to be heated 102, and the latent heat of condensation heats the object to be heated 102. Further, as the amount of steam decreases due to the condensation of the steam 108, the pressure around the object to be heated 102 decreases, so that a pressure distribution occurs in the steam heating furnace 101. Then, due to the pressure difference, the steam 108 existing above the object to be heated 102 is attracted in the direction approaching the object to be heated 102, and the height of the steam surface 109 is lowered. Further, as the condensation of the steam 108 in the steam heating furnace 101 progresses, the pressure in the entire steam heating furnace 101 decreases, so that the partition portion 112 in the steam holding portion 111 is pushed by the pressure in the second space 114. The partition 112 moves upward.

仕切り部112の上方向への移動により、第1の空間113を満たしていた蒸気108が、接続口92を介して蒸気加熱炉101内に供給される。仕切り部112の移動は、被加熱物102の温度が蒸気108の温度に到達し、蒸気108の凝縮が終わり、蒸気加熱炉101内の圧力が一定になるか、仕切り部112が固定部115に到達するまで、継続する。そして、仕切り部112が上向きに移動している間は、第1の空間113から蒸気加熱炉101内への蒸気108の供給は、継続する。 By moving the partition portion 112 upward, the steam 108 filling the first space 113 is supplied into the steam heating furnace 101 via the connection port 92. As for the movement of the partition portion 112, the temperature of the object to be heated 102 reaches the temperature of the steam 108, the condensation of the steam 108 is completed, the pressure in the steam heating furnace 101 becomes constant, or the partition portion 112 is moved to the fixed portion 115. Continue until you reach it. Then, while the partition portion 112 is moving upward, the supply of steam 108 from the first space 113 into the steam heating furnace 101 continues.

このように、被加熱物102の加熱の際の蒸気108の凝縮による蒸気加熱炉101内の圧力減少を利用し、余分な時間を要することなく、第1の空間113内に蓄えられていた蒸気108を、蒸気108が減少した分だけ蒸気加熱炉101内へ供給することができる。 In this way, the steam stored in the first space 113 without requiring extra time by utilizing the pressure decrease in the steam heating furnace 101 due to the condensation of the steam 108 when the object to be heated 102 is heated. The 108 can be supplied into the steam heating furnace 101 by the amount of the decrease of the steam 108.

被加熱物102の加熱が完了した後は、被加熱物102を載せた第2搬送ステージ103Bを、搬送位置の高さまで上昇させ、前述したように加熱準備室104を経由して、気相式加熱装置外へ被加熱物102が搬出される。 After the heating of the object to be heated 102 is completed, the second transfer stage 103B on which the object to be heated 102 is placed is raised to the height of the transfer position, and as described above, the gas phase type is passed through the heating preparation chamber 104. The object to be heated 102 is carried out of the heating device.

蒸気保持部111と蒸気加熱炉101との接続口92の下端は、被加熱物102の加熱時の加熱位置の被加熱物102の下端より上方に、例えば、加熱時の被加熱物102の下端の高さと同等以上の高さに配置される。また、接続口92の上端は、冷却コイル110より下方で、例えば、冷却コイル110の高さ以下の高さで、且つ被加熱物102の加熱時の加熱位置の被加熱物102の上端より上方に配置される。 The lower end of the connection port 92 between the steam holding portion 111 and the steam heating furnace 101 is above the lower end of the heated object 102 at the heating position when the heated object 102 is heated, for example, the lower end of the heated object 102 during heating. It is placed at a height equal to or higher than the height of. Further, the upper end of the connection port 92 is below the cooling coil 110, for example, at a height equal to or lower than the height of the cooling coil 110 and above the upper end of the heated object 102 at the heating position when the heated object 102 is heated. Is placed in.

このような構成により、蒸気加熱炉101内の冷却コイル110より下方の空間が蒸気108で満たされているときは、第1の空間113と第2の空間114との圧力差に基づく仕切り部112の移動により、第2の空間114の容積が減少し、第1の空間113に蒸気が取り込まれる。一方、蒸気加熱炉101内の蒸気が減少したときは、第1の空間113と第2の空間114との間の圧力差に基づく仕切り部112の移動により、第2の空間114の容積が増加し、第1の空間113に取り込まれて保持されていた蒸気を、蒸気加熱炉101内に供給することができる。 With such a configuration, when the space below the cooling coil 110 in the steam heating furnace 101 is filled with steam 108, the partition portion 112 based on the pressure difference between the first space 113 and the second space 114 Due to the movement of the second space 114, the volume of the second space 114 is reduced, and steam is taken into the first space 113. On the other hand, when the steam in the steam heating furnace 101 decreases, the volume of the second space 114 increases due to the movement of the partition portion 112 based on the pressure difference between the first space 113 and the second space 114. Then, the steam taken in and held in the first space 113 can be supplied into the steam heating furnace 101.

被加熱物102に対する所望の加熱を実施するために、第2の空間114の初期の容積は、熱転移液106の種類と、被加熱物102の加熱に必要な蒸気量と、蒸気加熱炉101内の容積とから設定される。 In order to carry out the desired heating of the object to be heated 102, the initial volume of the second space 114 is the type of the heat transfer liquid 106, the amount of steam required to heat the object to be heated 102, and the steam heating furnace 101. It is set from the volume inside.

一例として、蒸発潜熱62.7J/g、沸点270℃であるフッ素系熱転移液を使用し、熱容量30J/Kの被加熱物102を20℃から270℃まで加熱する場合について、以下、説明する。前記の加熱に必要な熱量は、7500Jとなるので、必要な蒸気量は、120gとなる。フッ素系熱転移液の270℃における蒸気密度は22kg/mとすると、被加熱物102を270℃まで加熱するのに必要な蒸気108の容積は、5.5Lである。ここで、所望の加熱に必要な蒸気108の容積の6割の3.3L分は、蒸気加熱炉101内の加熱位置の被加熱物102の上端の高さより上方にある初期の蒸気108で賄うとして、残りの4割の2.2L分を、第1の空間113内に蓄えるものとする。すなわち、仕切り部112が固定部115の高さに位置しているときの第2の空間114の容積と、蒸気108を第1の空間113内に所望の加熱に必要な蒸気量を蓄えたときの第2の空間114の容積との差を、2.2Lとする。第2の空間114の初期の体積をV、圧力をP、所望の加熱に必要な蒸気108を第1の空間113内に蓄えたときの第2の空間114の体積をV、圧力をPとすると蒸気を満たすために、P×(V/V)=P、V−V=2.2L が成り立つ。第2の空間114の初期の圧力Pは、前述のように大気圧に対して数Pa程度正圧に設定されており、仮に10Pa正圧に設定されているとし、標準状態の大気圧を1.013×10^5Paとして計算すると、第2の空間114の初期の圧力Pは、1.014×10^5Paである。また、所望の加熱に必要な蒸気108を第1の空間113内に蓄えたときの第2の空間114の圧力Pは、そのときの蒸気加熱炉101内の圧力と平衡状態にあり、蒸気加熱炉101内の圧力は、蒸気加熱炉101内の温度が熱転移液106の沸点温度に達しており、沸点における蒸気圧分上昇していることから、2.026×10^5Pa程度になっている。 As an example, a case where a fluorine-based thermal transfer liquid having a latent heat of vaporization of 62.7 J / g and a boiling point of 270 ° C. is used to heat an object to be heated 102 having a heat capacity of 30 J / K from 20 ° C. to 270 ° C. will be described below. .. Since the amount of heat required for the above heating is 7500 J, the required amount of steam is 120 g. Assuming that the vapor density of the fluorine-based thermal transfer liquid at 270 ° C. is 22 kg / m 3 , the volume of steam 108 required to heat the object to be heated 102 to 270 ° C. is 5.5 L. Here, 3.3 L, which is 60% of the volume of steam 108 required for desired heating, is covered by the initial steam 108 located above the height of the upper end of the object to be heated 102 at the heating position in the steam heating furnace 101. As a result, the remaining 40% of 2.2 L is stored in the first space 113. That is, when the volume of the second space 114 when the partition portion 112 is located at the height of the fixed portion 115 and the amount of steam required for desired heating of the steam 108 are stored in the first space 113. The difference from the volume of the second space 114 is 2.2 L. The initial volume of the second space 114 is V 0 , the pressure is P 0 , and the volume of the second space 114 when the steam 108 required for the desired heating is stored in the first space 113 is V 1 , the pressure. When is P 1 , P 0 × (V 0 / V 1 ) = P 1 and V 0 −V 1 = 2.2 L are established in order to satisfy the steam. Assuming that the initial pressure P 0 of the second space 114 is set to a positive pressure of about several Pa with respect to the atmospheric pressure as described above, and is set to a positive pressure of 10 Pa, the atmospheric pressure in the standard state is set. When calculated as 1.013 × 10 ^ 5 Pa, the initial pressure P 0 of the second space 114 is 1.014 × 10 ^ 5 Pa. Further, the pressure P 1 of the second space 114 when the steam 108 required for desired heating is stored in the first space 113 is in equilibrium with the pressure in the steam heating furnace 101 at that time, and is steam. The pressure in the heating furnace 101 is about 2.026 × 10 ^ 5 Pa because the temperature in the steam heating furnace 101 has reached the boiling point temperature of the thermal transfer liquid 106 and the vapor pressure at the boiling point has increased. ing.

以上から、第2の空間114の初期の体積V、所望の加熱に必要な蒸気108を第1の空間113内に蓄えたときの第2の空間114の体積Vを計算すると、V=4.4L、V=2.2L程度に設定すればよい。 From the above, when the initial volume V 0 of the second space 114 and the volume V 1 of the second space 114 when the steam 108 required for desired heating is stored in the first space 113 are calculated, V 0. It may be set to about 4.4L and V 1 = 2.2L.

前記実施形態によれば、蒸気加熱炉101の側部に蒸気を蓄える空間として蒸気保持部111を設け、被加熱物102の加熱によって蒸気量が減少した際に、蒸気量の減少に伴う炉内の圧力変化を一定に保持するように、蒸気を蓄える空間である蒸気保持部111の容積を変化させる機構として蒸気保持部111を設けている。このため、被加熱物102の加熱により蒸気加熱炉101内の蒸気量が減少した際に、蒸気加熱炉101の側部に設置した、蒸気を蓄える空間である蒸気保持部111から、蒸気108を被加熱物近傍に即時に供給することができ、プロセス時間を短縮することが可能となる。 According to the above embodiment, the steam holding portion 111 is provided as a space for storing steam on the side portion of the steam heating furnace 101, and when the steam amount is reduced by heating the object to be heated 102, the inside of the furnace is accompanied by the decrease in the steam amount. The steam holding unit 111 is provided as a mechanism for changing the volume of the steam holding unit 111, which is a space for storing steam, so as to keep the pressure change of the above constant. Therefore, when the amount of steam in the steam heating furnace 101 decreases due to the heating of the object to be heated 102, the steam 108 is transferred from the steam holding portion 111, which is a space for storing steam, installed on the side of the steam heating furnace 101. It can be immediately supplied to the vicinity of the object to be heated, and the process time can be shortened.

なお、本発明は前記実施形態に限定されるものではなく、その他種々の態様で実施できる。例えば、図6のように蒸気保持部111を二つ以上設置することで、蒸気保持部111一つ当たりの容積を、蒸気保持部111の数だけ分割し、小さくしてもよい。 The present invention is not limited to the above embodiment, and can be implemented in various other aspects. For example, by installing two or more steam holding portions 111 as shown in FIG. 6, the volume per steam holding portion 111 may be divided by the number of steam holding portions 111 to be reduced.

なお、前記様々な実施形態又は変形例のうちの任意の実施形態又は変形例を適宜組み合わせることにより、それぞれの有する効果を奏するようにすることができる。また、実施形態同士の組み合わせ又は実施例同士の組み合わせ又は実施形態と実施例との組み合わせが可能であると共に、異なる実施形態又は実施例の中の特徴同士の組み合わせも可能である。 In addition, by appropriately combining any embodiment or modification of the various embodiments or modifications, the effects of each can be achieved. Further, it is possible to combine the embodiments or the embodiments, or the embodiments and the embodiments, and also to combine the features in the different embodiments or the embodiments.

本発明の前記態様にかかる気相式加熱装置は、熱転移液の蒸気の減少による被加熱物近傍の圧力減少を駆動力として、蒸気保持部内の蒸気を即時に被加熱物近傍に供給できるため、被加熱物を短時間で所望の温度に昇温できる。そのため、本発明の前記態様は、高効率な加熱装置として、工業製品又は家電製品の製造工程又は各種電子部品の製造工程における乾燥炉、焼成炉、キュア炉、又はリフロー炉などの各種熱処理を行う熱処理装置に適用できる。 This is because the vapor phase heating device according to the above aspect of the present invention can immediately supply the steam in the steam holding portion to the vicinity of the object to be heated by using the pressure decrease in the vicinity of the object to be heated due to the decrease in the steam of the heat transfer liquid as a driving force. , The object to be heated can be heated to a desired temperature in a short time. Therefore, in the above aspect of the present invention, as a highly efficient heating device, various heat treatments such as a drying furnace, a firing furnace, a curing furnace, or a reflowing furnace are performed in the manufacturing process of industrial products or home appliances or the manufacturing process of various electronic parts. Applicable to heat treatment equipment.

1 蒸気槽
2 被加熱物
3 コンベア
4 ヒータ
5 熱転移液
6 温度センサ
6a 温度センサの先端
7 蒸気
8 搬入口
9 搬出口
10 加熱装置
11 電力調節器
90 外部空間
92 接続口
100 気相式加熱装置
101 蒸気加熱炉
101a 内部空間
102 被加熱物
103A 第1搬送ステージ
103B 第2搬送ステージ
104 加熱準備室
105A 第1シャッタ
105B 第2シャッタ
106 熱転移液
107 ヒータ
108 蒸気
109 蒸気面
110 冷却コイル
111 蒸気保持部
112 仕切り部
113 第1の空間
114 第2の空間
115 固定部
116 圧力調節接続部
117 圧力調節部
118 圧力制御部
119A 圧力計
119B 圧力計
1 Steam tank 2 Heated object 3 Conveyor 4 Heater 5 Heat transfer liquid 6 Temperature sensor 6a Tip of temperature sensor 7 Steam 8 Carry-in port 9 Carry-out port 10 Heating device 11 Power controller 90 External space 92 Connection port 100 Gas-phase heating device 101 Steam heating furnace 101a Internal space 102 Heated object 103A First transfer stage 103B Second transfer stage 104 Heating preparation chamber 105A First shutter 105B Second shutter 106 Heat transfer liquid 107 Heater 108 Steam 109 Steam surface 110 Cooling coil 111 Steam retention Part 112 Partition part 113 First space 114 Second space 115 Fixed part 116 Pressure adjustment connection part 117 Pressure adjustment part 118 Pressure control part 119A Pressure gauge 119B Pressure gauge

Claims (3)

熱転移液の蒸気の凝縮潜熱を利用して被加熱物を加熱する気相式加熱装置であって、
外部空間から内部空間が遮断される蒸気加熱炉と、
前記蒸気加熱炉に前記蒸気を供給する蒸気供給部と、
前記蒸気加熱炉で加熱位置と搬送位置との間で前記被加熱物を搬送する搬送部と、
前記蒸気加熱炉で、前記加熱位置の前記被加熱物の上端より上方に設けられた冷却部と、
前記蒸気加熱炉の側部に設けられて前記蒸気加熱炉と接続口を介して連通可能に前記蒸気を蓄える蒸気保持部とを有し、
前記蒸気保持部は、
前記蒸気加熱炉に連通する第1の空間と、
内部空間の容積が変化することにより前記第1の空間の容積を変化させる第2の空間と、
前記第1の空間と前記第2の空間とを仕切る仕切り部とを有し、
前記蒸気保持部と前記蒸気加熱炉とを接続する前記接続口の下端の高さは、前記被加熱物の前記加熱位置の前記被加熱物の下端より上方に配置され、前記接続口の上端の高さは、前記冷却部より下方で、且つ前記被加熱物の前記加熱位置の前記被加熱物の上端より上方に配置され、
前記蒸気加熱炉内の前記冷却部より下方の空間が前記蒸気で満たされているときは、前記仕切り部の移動により前記第2の空間の容積が減少し、前記第1の空間に前記蒸気が取り込まれ、前記蒸気加熱炉内の前記蒸気が減少したときは、前記第1の空間と前記第2の空間との間の圧力差に基づく前記仕切り部の移動により、前記第2の空間の容積が増加し、前記第1の空間に取り込まれた前記蒸気を前記蒸気加熱炉内に供給する、気相式加熱装置。
It is a vapor phase heating device that heats the object to be heated by utilizing the latent heat of condensation of the vapor of the thermal transfer liquid.
A steam heating furnace that cuts off the internal space from the external space,
A steam supply unit that supplies the steam to the steam heating furnace,
A transport unit that transports the object to be heated between the heating position and the transport position in the steam heating furnace, and
In the steam heating furnace, a cooling unit provided above the upper end of the object to be heated at the heating position and
It has a steam heating furnace provided on a side portion of the steam heating furnace and a steam holding portion for storing the steam so as to be able to communicate with each other through a connection port.
The steam holding part is
The first space communicating with the steam heating furnace and
A second space that changes the volume of the first space by changing the volume of the internal space, and
It has a partition portion that separates the first space from the second space.
The height of the lower end of the connection port connecting the steam holding portion and the steam heating furnace is arranged above the lower end of the heated object at the heating position of the heated object, and is located at the upper end of the connection port. The height is arranged below the cooling unit and above the upper end of the heated object at the heating position of the heated object.
When the space below the cooling portion in the steam heating furnace is filled with the steam, the volume of the second space is reduced by the movement of the partition portion, and the steam is filled in the first space. When the steam is taken in and the steam in the steam heating furnace is reduced, the volume of the second space is increased by the movement of the partition portion based on the pressure difference between the first space and the second space. Is increased, and the steam taken into the first space is supplied to the steam heating furnace.
前記蒸気保持部を2つ以上備える、請求項1に記載の気相式加熱装置。 The vapor phase heating device according to claim 1, further comprising two or more steam holding portions. 前記蒸気加熱炉と連通可能に配置し、内部の圧力を前記蒸気加熱炉内の圧力と前記蒸気加熱炉外の圧力との間で調節できる加熱準備室をさらに備えて、前記蒸気加熱炉外の圧力での前記加熱準備室を介して、前記被加熱物を前記蒸気加熱炉外と前記加熱準備室との間で移動可能とし、前記蒸気加熱炉内の圧力での前記加熱準備室を介して、前記被加熱物を前記蒸気加熱炉内と前記加熱準備室との間で移動可能とする、請求項1又は2に記載の気相式加熱装置。 The outside of the steam heating furnace is further provided with a heating preparation chamber which is arranged so as to be communicable with the steam heating furnace and can adjust the internal pressure between the pressure inside the steam heating furnace and the pressure outside the steam heating furnace. The object to be heated can be moved between the outside of the steam heating furnace and the heating preparation chamber through the heating preparation chamber at pressure, and through the heating preparation chamber at pressure inside the steam heating furnace. The vapor-phase heating device according to claim 1 or 2, wherein the object to be heated can be moved between the steam heating furnace and the heating preparation chamber.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62151267A (en) * 1985-12-26 1987-07-06 Tamura Seisakusho Co Ltd Vapor phase type soldering device
JPS6444275A (en) * 1987-08-10 1989-02-16 Tamura Seisakusho Kk Vapor phase soldering device
JP2004327816A (en) * 2003-04-25 2004-11-18 Denso Corp Method and device for reflow soldering
JP2020076540A (en) * 2018-11-07 2020-05-21 パナソニックIpマネジメント株式会社 Gas phase type heating method and gas phase type heating device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62151267A (en) * 1985-12-26 1987-07-06 Tamura Seisakusho Co Ltd Vapor phase type soldering device
JPS6444275A (en) * 1987-08-10 1989-02-16 Tamura Seisakusho Kk Vapor phase soldering device
JP2004327816A (en) * 2003-04-25 2004-11-18 Denso Corp Method and device for reflow soldering
JP2020076540A (en) * 2018-11-07 2020-05-21 パナソニックIpマネジメント株式会社 Gas phase type heating method and gas phase type heating device

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