JPH102801A - Temperature detection method of the object to be heated in infrared heating furnace - Google Patents
Temperature detection method of the object to be heated in infrared heating furnaceInfo
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- JPH102801A JPH102801A JP15237796A JP15237796A JPH102801A JP H102801 A JPH102801 A JP H102801A JP 15237796 A JP15237796 A JP 15237796A JP 15237796 A JP15237796 A JP 15237796A JP H102801 A JPH102801 A JP H102801A
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- heated
- temperature
- infrared
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- heater
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Abstract
(57)【要約】
【課題】 赤外線加熱炉内の被加熱体の温度検知方法に
関し、計算のみで定量的に精度よく検知することを課題
とする。
【解決手段】 赤外線ヒータを有する加熱炉内の被加熱
体の温度を数値解析によって検知する際に、赤外線の波
長域を複数の範囲に分割し、それぞれの分割した波長域
毎に、被加熱体がヒータから受けるふく射熱量と周囲に
放射するふく射熱量との収支を計算し、これらを合算し
て被加熱体が炉内で受ける正味のふく射熱量を計算し、
これを境界条件として被加熱体の熱解析を行い、被加熱
体の温度を検知する。
(57) [Summary] [PROBLEMS] To detect a temperature of an object to be heated in an infrared heating furnace by quantitatively and accurately detecting the temperature only by calculation. SOLUTION: When detecting the temperature of an object to be heated in a heating furnace having an infrared heater by numerical analysis, the wavelength range of infrared rays is divided into a plurality of ranges, and the object to be heated is divided for each of the divided wavelength ranges. Calculate the balance between the amount of radiant heat received from the heater and the amount of radiant heat radiated to the surroundings, and add these to calculate the net radiant heat received by the heated body in the furnace,
Using this as a boundary condition, a thermal analysis of the object to be heated is performed to detect the temperature of the object to be heated.
Description
【0001】[0001]
【発明の属する技術分野】この発明は、赤外線加熱炉内
の被加熱体の温度検知方法に関する。The present invention relates to a method for detecting the temperature of an object to be heated in an infrared heating furnace.
【0002】[0002]
【従来の技術】赤外線加熱は被加熱体を直接かつ瞬時に
熱することが出来るため、工業、医療、食品加工など幅
広い分野において効率がよく、付加価値の高い加熱方式
として注目されている。電子機器の分野では、プリント
板上に電子部品をはんだ付けする実装工程において、は
んだを溶融するため赤外線ヒータにより加熱する方式の
赤外線リフロー炉と呼ばれる加熱炉を用いる。2. Description of the Related Art Infrared heating is capable of directly and instantaneously heating an object to be heated, and is therefore attracting attention as a high-value-added heating method that is efficient in a wide range of fields such as industrial, medical, and food processing. In the field of electronic devices, in a mounting step of soldering electronic components onto a printed board, a heating furnace called an infrared reflow furnace of a method of heating with an infrared heater to melt the solder is used.
【0003】しかし、赤外線加熱は局所的な加熱に不向
きであることや、被加熱体の材質の違いにより赤外線吸
収特性が異なるなどの理由から、プリント板を均一に加
熱し、はんだ接合部が適切な温度になるように赤外線ヒ
ータの温度や加熱時間などの条件を設定するのは難し
い。However, because the infrared heating is not suitable for local heating and the infrared absorption characteristics are different due to the difference in the material of the object to be heated, the printed board is uniformly heated and the solder joints are appropriately heated. It is difficult to set conditions such as the temperature of the infrared heater and the heating time so that the temperature becomes appropriate.
【0004】このため、新規のプリント板に対する前記
加熱条件の設定は、熱電体などによるプリント配線板の
温度の実測、および作業者の経験や勘による赤外線ヒー
タの温度や加熱時間などの条件設定を数回繰り返して、
はんだ接合部が目標の温度となるようにしていた。しか
し、この様な前記加熱条件の設定方法では、設定に多く
の時間を要し作業製が極めて悪く、また経験の浅い作業
者がこれらの設定を行う場合には尚更である。[0004] For this reason, the setting of the heating conditions for a new printed board is performed by actually measuring the temperature of the printed wiring board using a thermoelectric body or the like, and setting conditions such as the temperature and heating time of the infrared heater based on the experience and intuition of the operator. Repeat several times,
The solder joint was set to the target temperature. However, such a method for setting the heating conditions requires a lot of time for setting and is extremely poor in work quality, and is even more difficult when an inexperienced operator performs these settings.
【0005】このため、赤外線加熱炉内の被加熱体の温
度分布を数値解析によって予測し、これを赤外線加熱炉
の加熱条件の設定に利用することが一部で行われつつあ
る。しかし、従来の方法では、赤外線ヒータの放射エネ
ルギの波長分布や被加熱体の吸収率の波長分布のマッチ
ングが、被加熱体の温度上昇の度合に大きく影響するに
もかかわらず、これを無視し、放射率や吸収率が波長に
依存せず一定とし、平均値を用いて計算(灰色体として
計算)するようにしている。[0005] For this reason, the temperature distribution of the object to be heated in the infrared heating furnace is predicted by numerical analysis, and the prediction is used in part for setting heating conditions of the infrared heating furnace. However, in the conventional method, although the matching of the wavelength distribution of the radiant energy of the infrared heater and the wavelength distribution of the absorptance of the object to be heated greatly affects the degree of temperature rise of the object to be heated, it is ignored. The emissivity and the absorptance are constant without depending on the wavelength, and are calculated using the average value (calculated as a gray body).
【0006】また、赤外線ヒータから被加熱体に届くエ
ネルギの割合(形態係数)が加熱炉の状態により様々で
あるがこれを考慮できない。また、被加熱体がベルト・
コンベアなどに載って炉内を移動する場合には形態係数
は時間と共に変化するが、計算を簡単にするためこれを
一定として計算するなど、定量的な解析精度を決定する
重要な要素であるふく射計算を簡略的に扱うものであっ
た。Further, the ratio (view factor) of the energy reaching the object to be heated from the infrared heater varies depending on the state of the heating furnace, but this cannot be taken into account. The object to be heated is a belt
When moving in a furnace on a conveyor, etc., the view factor changes with time, but radiation is an important factor in determining quantitative analysis accuracy, such as calculating this constant for ease of calculation. The calculations were simplified.
【0007】[0007]
【発明が解決しようとする課題】このため従来のふく射
計算方法を用いた赤外線リフロー炉内のプリント板の熱
解析による結果は、実際のリフロー炉内のプリント板の
温度分布やこの時間変化と比較すると定量的な正確さに
欠け、この解析結果のみからリフロー炉内の赤外線ヒー
タの温度や加熱時間(コンベア速度)等のプリント板の
加熱条件を決定するのは困難であるといった問題を生じ
ていた。For this reason, the result of thermal analysis of a printed board in an infrared reflow furnace using the conventional radiation calculation method is compared with the actual temperature distribution of the printed board in the reflow furnace and its time change. Then, there was a problem that the quantitative accuracy was lacking, and it was difficult to determine the heating conditions of the printed board such as the temperature of the infrared heater in the reflow furnace and the heating time (conveyor speed) based on only the analysis results. .
【0008】この発明は、このような事情を考慮してな
されたもので、赤外線リフロー炉内のプリント配線板の
温度分布やこの時間変化(温度プロファイル)を、数値
解析により精度よく検知する方法を提供するものであ
る。The present invention has been made in view of such circumstances, and provides a method for accurately detecting the temperature distribution of a printed wiring board in an infrared reflow furnace and its time change (temperature profile) by numerical analysis. To provide.
【0009】[0009]
【課題を解決するための手段】この発明は、赤外線ヒー
タを有する加熱炉内の被加熱体の温度を数値解析によっ
て検知する際に、赤外線の波長域を複数の範囲に分割
し、それぞれの分割した波長域毎に、被加熱体がヒータ
から受けるふく射熱量と周囲に放射するふく射熱量との
収支を計算し、これらを合算して被加熱体が炉内で受け
る正味のふく射熱量を計算し、これを境界条件として被
加熱体の熱解析を行い、被加熱体の温度を検知すること
を特徴とする赤外線加熱炉内の被加熱体の温度検知方法
を提供するものである。SUMMARY OF THE INVENTION The present invention divides an infrared wavelength range into a plurality of ranges when detecting the temperature of an object to be heated in a heating furnace having an infrared heater by numerical analysis. For each of the wavelength ranges that have been calculated, calculate the balance between the amount of radiant heat received by the object to be heated from the heater and the amount of radiant heat radiated to the surroundings, and add these to calculate the net amount of radiated heat received by the object to be heated in the furnace, An object of the present invention is to provide a method for detecting a temperature of a heated object in an infrared heating furnace, wherein the temperature of the heated object is detected by performing a thermal analysis of the heated object using this as a boundary condition.
【0010】[0010]
【発明の実施の形態】この発明において、赤外線加熱炉
内の赤外線ヒータから放射されたふく射エネルギが被加
熱体へ届く割合を示す値である形態係数は、被加熱体が
コンベアなどに載って炉内を移動し赤外線ヒータとの相
対的に位置が変化する場合には、非定常解析のタイムス
テップ(時間増分)毎あるいは複数のタイムステップ毎
に計算し、この値を用いて赤外線ヒータから被加熱体が
受けるふく射熱量を計算し、これと被加熱体自身が放射
するふく射熱量との収支計算を行い、被加熱体が受ける
正味のふく射熱量を境界条件として被加熱体の熱伝導解
析を行い、被加熱体の温度分布やこの時間変化を知るよ
うにする。DESCRIPTION OF THE PREFERRED EMBODIMENTS In the present invention, a view factor, which is a value indicating a ratio of radiation energy radiated from an infrared heater in an infrared heating furnace to a heated object, is referred to as a furnace coefficient when the heated object is placed on a conveyor or the like. If the position changes relative to the infrared heater due to movement within the interior, it is calculated for each time step (time increment) of the unsteady analysis or for each of a plurality of time steps. Calculate the amount of radiant heat received by the body, calculate the balance between this and the amount of radiant heat radiated by the heated object itself, and analyze the heat conduction of the heated object using the net amount of radiated heat received by the heated object as a boundary condition, The temperature distribution of the object to be heated and its time change are known.
【0011】また、赤外線ヒータから被加熱体が受ける
ふく射熱量と被加熱体自身が周囲に放射するふく射熱量
の計算において、赤外線ヒータや被加熱体のふく射エネ
ルギ強度の波長分布と放射率、吸収率の波長分布を赤外
線の波長域で複数個に分割し、それぞれの分割した波長
域における被加熱体へのふく射熱量の収支を計算し、最
後にこれらの分割した波長域における収支を合算する。In calculating the amount of radiant heat received by the object to be heated from the infrared heater and the amount of radiant heat radiated to the surroundings of the object itself, the wavelength distribution, emissivity, and absorptance of the radiant energy of the infrared heater and the object to be heated are calculated. Is divided into a plurality of wavelength distributions in the infrared wavelength range, the balance of the amount of heat radiated to the object to be heated in each of the divided wavelength ranges is calculated, and finally, the balance in these divided wavelength ranges is added.
【0012】解析結果の精度を更に高めるためには、赤
外線ヒータと被加熱体との間の形態係数以外に、炉内壁
面と被加熱体との間の形態係数を計算し、これを用いて
炉内壁面から被加熱体が受けるふく射熱量を計算し、収
支計算に加算してもよい。In order to further improve the accuracy of the analysis result, in addition to the view factor between the infrared heater and the object to be heated, the view factor between the inner wall of the furnace and the object to be heated is calculated and used. The amount of radiant heat received by the object to be heated from the furnace inner wall surface may be calculated and added to the balance calculation.
【0013】また、赤外線ヒータから炉内壁面で反射し
て被加熱体に至る形態係数を計算し、これを用いて赤外
線ヒータから炉内壁面で反射して被加熱体に届くふく射
熱量を計算し、収支計算に加算することで被加熱体が受
ける正確なふく射熱量を計算することができる。Further, a view factor which is reflected from the infrared heater on the inner wall surface of the furnace and reaches the object to be heated is calculated, and a radiation heat amount which is reflected from the infrared heater on the inner wall surface of the furnace and reaches the object to be heated is calculated. , The accurate amount of radiation heat received by the object to be heated can be calculated.
【0014】また、これらの炉内壁面が関係するふく射
計算においても、赤外線ヒータ、炉内壁面、被加熱体の
それぞれがもつふく射エネルギ強度の波長分布と放射
率、吸収率、反射率の波長分布を赤外線の波長域で複数
個に分割し、それぞれの分割した波長域における被加熱
体へのふく射熱量の収支を計算し、最後にこれら分割し
た波長域における収支を合算することで、被加熱体が炉
内で受ける正味のふく射熱量を計算してもよい。In the radiation calculation relating to the inner wall of the furnace, the wavelength distribution of the radiation energy and the wavelength distribution of the emissivity, absorptivity, and reflectance of the infrared heater, the inner wall of the furnace, and the object to be heated are also obtained. Is divided into a plurality of parts in the infrared wavelength range, the balance of the amount of radiation heat to the heated body in each of the divided wavelength ranges is calculated, and finally, the balance in these divided wavelength ranges is added up, thereby obtaining the heated body. May calculate the net radiant heat received in the furnace.
【0015】以下にこれらの計算をパーソナルコンピュ
ータを用いて実行する場合について詳述する。ここで、
図1に示すように、赤外線加熱炉内に各ヒータJHEAT,IH
EATがX方向に配列され、その中を被加熱体すなわちプ
リント板PCBが炉入口(X=0)から出口へ向ってX方
向に移動するものとする。Hereinafter, a case where these calculations are performed using a personal computer will be described in detail. here,
As shown in FIG. 1, each heater JHEAT, IH
It is assumed that EATs are arranged in the X direction, in which the object to be heated, that is, the printed circuit board PCB, moves in the X direction from the furnace inlet (X = 0) to the outlet.
【0016】計算手順の概要を図2のフローチャートを
用いて説明する。最初に時系列でない(タイムステップ
を通じて一定である)形態係数を計算し、その他の時系
列でない値である、ヒータの放射エネルギ、炉の周囲壁
面の放射エネルギを計算する(ステップS1〜S3)。An outline of the calculation procedure will be described with reference to the flowchart of FIG. First, a non-time-series (constant throughout the time step) view factor is calculated, and other non-time-series values, that is, the radiant energy of the heater and the radiant energy of the peripheral wall surface of the furnace are calculated (steps S1 to S3).
【0017】次に、各タイムステップ毎の計算を開始す
る。各タイムステップのはじめには時系列の(各タイム
ステップにより変化する)形態係数を計算する(ステッ
プS4)。次に計算要素がヒータおよび炉内の周囲壁面
から直接受けるエネルギを計算し、ヒータから周囲壁面
で反射して計算要素が受けるエネルギを算出する(ステ
ップS5,S6)。次に、計算要素が放射により失うエ
ネルギを計算したあと、計算要素に関するエネルギの収
支を算出する(ステップS7〜S9)。Next, the calculation for each time step is started. At the beginning of each time step, a time-series view factor (which changes with each time step) is calculated (step S4). Next, the calculation element calculates the energy directly received from the heater and the surrounding wall surface in the furnace, and calculates the energy reflected on the surrounding wall surface from the heater and received by the calculation element (steps S5 and S6). Next, after calculating the energy that the calculation element loses due to radiation, the energy balance of the calculation element is calculated (steps S7 to S9).
【0018】以上の計算が全計算要素について終了する
と(ステップS10)、これによって計算された熱量を
各計算要素が受けるふく射境界条件として、このタイム
ステップの最後にプリント板の熱伝導解析を行う(ステ
ップS11)。次にこのタイムステップをプリント板が
炉の入口から出口まで進む間、繰り返し実行し計算を終
了する(ステップS12)。When the above calculation is completed for all the calculation elements (step S10), the heat quantity thus calculated is used as a radiation boundary condition that each calculation element receives, and a heat conduction analysis of the printed board is performed at the end of this time step (step S10). Step S11). Next, this time step is repeatedly executed while the printed board advances from the entrance to the exit of the furnace, and the calculation is completed (step S12).
【0019】次に、図2におけるステップS1〜S10
について、図3〜図11に示すフローチャートと共に説
明する。まず、図3に示す時系列でない形態係数の計算
を実行する。予め、ヒータおよび炉内壁面の面積の計算
をしておく。 AHEAT = LHEAT * WHEAT AWALL = 2.0 *(LWALL * WWALL + LWALL * HWALL + WW
ALL * HWALL)- 8.0 * AHEATNext, steps S1 to S10 in FIG.
Will be described with reference to the flowcharts shown in FIGS. First, calculation of a view factor that is not a time series shown in FIG. 3 is performed. The areas of the heater and the inner wall of the furnace are calculated in advance. AHEAT = LHEAT * WHEAT AWALL = 2.0 * (LWALL * WWALL + LWALL * HWALL + WW
ALL * HWALL)-8.0 * AHEAT
【0020】ここで、 AHEAT : ヒータの面積 LHEAT : ヒータの長さ WHEAT : ヒータの幅 AWALL : 炉内壁面の面積 LWALL : 炉内壁面の長さ WWALL : 炉内壁面の幅 HWALL : 炉内壁面の高さ である。Here, AHEAT: area of heater LHEAT: length of heater WHEAT: width of heater AWALL: area of furnace inner wall LWALL: length of furnace inner wall WWALL: width of furnace inner wall HWALL: width of furnace inner wall Height.
【0021】そして、時系列でない形態係数に関する計
算を次の要領で行う。 (1) ヒータのX座標の算出 HPOS(IHEAT) = LPRE + (IHEAT-1) * (LHEAT + LBET) +
LHEAT * 0.5 ここで、 IHEAT : 入口からIHEAT 番目のヒータ HPOS(IHEAT) :IHEATの中心のX座標(入口 X=0) LPRE :入口から最初のヒータの前端までの距離 LBET :ヒータとヒータとの間の距離 である。Then, the calculation regarding the view factor which is not a time series is performed in the following manner. (1) Calculation of heater X coordinate HPOS (IHEAT) = LPRE + (IHEAT-1) * (LHEAT + LBET) +
LHEAT * 0.5 Where, IHEAT: IHEAT-th heater from entrance HPOS (IHEAT): X coordinate of the center of IHEAT (entrance X = 0) LPRE: Distance from entrance to front end of first heater LBET: Distance between heater and heater The distance between them.
【0022】(2) ヒータ間の位置関係の算出 HPOS1(IHEAT,JHEAT) = (IHEAT-1) * (LHEAT + LBET) +
LHEAT * 0.5-(JHEAT-1) * (LHEAT + LBET) HPOS2(IHEAT,JHEAT) = (IHEAT-1) * (LHEAT + LBET) +
LHEAT * 0.5-(JHEAT-1) * (LHEAT + LBET) ここで、 HPOS1(IHEAT,JHEAT) :IHEAT の中央点からJHEAT の後端
までのX方向の距離 HPOS2(IHEAT,JHEAT) :IHEAT の中央点からJHEAT の前端
までのX方向の距離 JHEAT : 上面ヒータ(1〜4) IHEAT : 下面ヒータ(1〜4) である。(2) Calculation of positional relationship between heaters HPOS1 (IHEAT, JHEAT) = (IHEAT-1) * (LHEAT + LBET) +
LHEAT * 0.5- (JHEAT-1) * (LHEAT + LBET) HPOS2 (IHEAT, JHEAT) = (IHEAT-1) * (LHEAT + LBET) +
LHEAT * 0.5- (JHEAT-1) * (LHEAT + LBET) where, HPOS1 (IHEAT, JHEAT): Distance in the X direction from the center point of IHEAT to the rear end of JHEAT HPOS2 (IHEAT, JHEAT): Center of IHEAT The distance in the X direction from the point to the front end of JHEAT. JHEAT: Upper heater (1-4) IHEAT: Lower heater (1-4).
【0023】(3) ヒータ間の形態係数の算出 SFHH(IHEAT,JHEAT) = 2.0 * (SFBASE(DISTZ * 2.0, HPO
S1(IHEAT,JHEAT), WHEAT/2.0) - SFBASE(DISTZ * 2.0,
HPOS2(IHEAT,JHEAT),WHEAT/2.0)) 関数SFBASE(A,B,C)を次のようにおく。 SFBASE(A,B,C) = ((B/(A2+B2)0.5)*sin-1(C/(A2+B2+C2)
0.5)+(C/((A2+C2)0.5)*sin-1(B/(A2+B2+C2)0.5)/2π(3) Calculation of view factor between heaters SFHH (IHEAT, JHEAT) = 2.0 * (SFBASE (DISTZ * 2.0, HPO
S1 (IHEAT, JHEAT), WHEAT / 2.0)-SFBASE (DISTZ * 2.0,
HPOS2 (IHEAT, JHEAT), WHEAT / 2.0)) The function SFBASE (A, B, C) is set as follows. SFBASE (A, B, C) = ((B / (A 2 + B 2 ) 0.5 ) * sin -1 (C / (A 2 + B 2 + C 2 )
0.5 ) + (C / ((A 2 + C 2 ) 0.5 ) * sin -1 (B / (A 2 + B 2 + C 2 ) 0.5 ) / 2π
【数1】 (Equation 1)
【0024】 (SFHH(1) = SFHH(4), SFHH(2) = SFHH(3)) ここで、 SFHH(IHEAT,JHEAT) :JHEATからIHEATへの形態係数 SFHH(JHEAT) :JHEATから向合う全てのヒータへの形態係
数 DISTZ : ヒータとPCB(コンベア中心線)との垂直方向
の距離 である。(SFHH (1) = SFHH (4), SFHH (2) = SFHH (3)) where, SFHH (IHEAT, JHEAT): a form factor from JHEAT to IHEAT SFHH (JHEAT): facing from JHEAT Form factor for all heaters DISTZ: This is the vertical distance between the heater and the PCB (conveyor center line).
【0025】(4) ヒータから周囲壁面への形態係数の算
出 SFHW(JHEAT) = 1.0 - SFHH(JHEAT) ここで、 SFHW(JHEAT) :JHEATから周囲壁面への形態係数 である。(4) Calculation of View Factor from Heater to Surrounding Wall Surface SFHW (JHEAT) = 1.0−SFHH (JHEAT) where SFHW (JHEAT) is the view factor from JHEAT to the surrounding wall surface.
【0026】(5) 周囲壁面から周囲壁面への形態係数の
算出 SFWW = 1.0 - 4.0 * AHEAT * (SFHW(1) + SFHW(2)) / A
WALL ここで、 SFWW :周囲壁面から周囲壁面への形態係数 である。(5) Calculation of view factor from surrounding wall surface to surrounding wall surface SFWW = 1.0-4.0 * AHEAT * (SFHW (1) + SFHW (2)) / A
WALL where SFWW is the view factor from the surrounding wall to the surrounding wall.
【0027】次に、図4に示す各ヒータの放射エネルギ
の計算を次の要領で行う。ここで、波長RAM=2〜27
μmとし、1μm毎に計算する。 QH(IHEAT,RAM) = (EPUH(IHEAT,RAM) * AHEAT * C1 * RA
M-5)/(exp(C2 / (RAM * THEAT(IHEAT))) -1) または、 QH(IHEAT) = EPUH(IHEAT) * AHEAT * SIG * THEAT(IHEA
T)4 Next, the calculation of the radiant energy of each heater shown in FIG. 4 is performed in the following manner. Here, wavelength RAM = 2 to 27
μm and calculate every 1 μm. QH (IHEAT, RAM) = (EPUH (IHEAT, RAM) * AHEAT * C1 * RA
M -5 ) / (exp (C2 / (RAM * THEAT (IHEAT))) -1) or QH (IHEAT) = EPUH (IHEAT) * AHEAT * SIG * THEAT (IHEA
T) 4
【0028】ここで、 IHEAT : 上下のヒータ(1〜8) RAM : 波長 QH(IHEAT,RAM) :IHEATが放射する波長RAMのエネルギ EPUH(IHEAT,RAM) :IHEATの波長RAMの放射率 C1 :定数(3.743*108) C2 :定数(1.4387*104) THEAT(IHEAT) :IHEATの温度 QH(IHEAT) :IHEATが放射するエネルギ EPUH(IHEAT) :IHEATの平均放射率 SIG : 定数(5.669*10-8) である。Here, IHEAT: upper and lower heaters (1 to 8) RAM: wavelength QH (IHEAT, RAM): energy of wavelength RAM radiated by IHEAT EPUH (IHEAT, RAM): emissivity of wavelength RAM of IHEAT C1: Constant (3.743 * 10 8 ) C2: Constant (1.4387 * 10 4 ) THEAT (IHEAT): Temperature of IHEAT QH (IHEAT): Energy radiated by IHEAT EPUH (IHEAT): Average emissivity of IHEAT SIG: Constant (5.669 * 10 -8 ).
【0029】次に、図5に示す周囲壁面の放射エネルギ
の計算を次の要領で行う。 QW(RAM) = (EPUW(RAM) * AWALL * C1 * RAM -5)/(exp(C
2 / (RAM * TWALL))-1 または QW = EPUW * AWALL * SIG * TWALL4 Next, the calculation of the radiant energy of the peripheral wall surface shown in FIG. 5 is performed in the following manner. QW (RAM) = (EPUW (RAM) * AWALL * C1 * RAM -5 ) / (exp (C
2 / (RAM * TWALL))-1 or QW = EPUW * AWALL * SIG * TWALL 4
【0030】ここで、 QW(RAM) : 壁面が放射する波長RAMのエネルギ EPUW(RAM) : 壁面の波長RAMの放射率 TWALL : 壁面の温度 QW :壁面が放射するエネルギ EPUW :壁面の平均放射率 である。Here, QW (RAM): energy of the wavelength RAM radiated by the wall EPUW (RAM): emissivity of the wavelength RAM of the wall TWALL: temperature of the wall QW: energy radiated by the wall EPUW: average emissivity of the wall It is.
【0031】次に、図6に示す時系列である形態係数に
関する計算を次の要領で行う。但し、計算はx秒毎に行
う。 (1) PCBの中心の座標などについての計算 PCBPOS = NTIME * VELOCI DELTAX(IHEAT) = HPOS(IHEAT) - PCBPOS L1(IHEAT) = DELTAX(IHEAT) - (LHEAT/2.0) L2(IHEAT) = DELTAX(IHEAT) + (LHEAT/2.0)Next, the calculation relating to the time-series view factors shown in FIG. 6 is performed in the following manner. However, the calculation is performed every x seconds. (1) Calculation about coordinates of center of PCB PCBPOS = NTIME * VELOCI DELTAX (IHEAT) = HPOS (IHEAT)-PCBPOS L1 (IHEAT) = DELTAX (IHEAT)-(LHEAT / 2.0) L2 (IHEAT) = DELTAX ( (IHEAT) + (LHEAT / 2.0)
【0032】ここで、 PCBPOS : PCBの中心のX座標(入口 X=0) NTIME : 現Time Stepにおける時刻 VELOCI :コンベアの速度 DELTAX(IHEAT) : IHEAT中心とPCBのX方向の距離 L1(IHEAT),L2(IHEAT) : PCBとIHEAT前端,後端との距離 である。Here, PCBPOS: X coordinate of the center of the PCB (entrance X = 0) NTIME: Time at the current Time Step VELOCI: Speed of the conveyor DELTAX (IHEAT): Distance between the center of IHEAT and the PCB in the X direction L1 (IHEAT) , L2 (IHEAT): The distance between the PCB and the front and rear ends of IHEAT.
【0033】(2) PCBからヒータへの形態係数の計算 SFPH(IHEAT) = 2.0 * (SFBASE(DISTZ,L2(IHEAT),WHEAT/
2.0)- SFBASE(DISTZ,L1(IHEAT),WHEAT/2.0)) ここで、 SFPH(IHEAT) :PCBからIHEATへの形態係数 である。(2) Calculation of view factor from PCB to heater SFPH (IHEAT) = 2.0 * (SFBASE (DISTZ, L2 (IHEAT), WHEAT /
2.0) -SFBASE (DISTZ, L1 (IHEAT), WHEAT / 2.0)) where SFPH (IHEAT) is a view factor from PCB to IHEAT.
【0034】(3) ヒータからPCBへの形態係数の計算 SFHP(IHEAT) = (APCB * SFPH(IHEAT))/AHEAT(3) Calculation of view factor from heater to PCB SFHP (IHEAT) = (APCB * SFPH (IHEAT)) / AHEAT
【数2】 (Equation 2)
【0035】ここで、 SFHP(IHEAT) :IHEATからPCBへの形態係数 APCB :PCBの面積 TSFHP : 上面の全てのヒータからPCBへの形態係数 である。Here, SFHP (IHEAT): View factor from IHEAT to PCB APCB: Area of PCB TSFHP: View factor from all heaters on the upper surface to PCB.
【0036】(4) 周囲壁面からPCBへの形態係数の計算 SFWP = (2.0 * APCB / AWALL) - (AHEAT / AWALL) * 2.
0 * TSFHP ここで、 SFWP :周囲壁面からPCBへの形態係数 である。(4) Calculation of view factor from surrounding wall surface to PCB SFWP = (2.0 * APCB / AWALL)-(AHEAT / AWALL) * 2.
0 * TSFHP where: SFWP: View factor from surrounding wall to PCB.
【0037】(5) ヒータから周囲壁面に反射してPCBに
届くエネルギの割合の計算 RHWP(IHEAT,RAM) = (ROHW(RAM) * SFWP * SFHW(IHEAT))
/ (1.0 - ROHW(RAM)* SFWW)(5) Calculation of the ratio of energy reflected from the heater to the surrounding wall and reaching the PCB RHWP (IHEAT, RAM) = (ROHW (RAM) * SFWP * SFHW (IHEAT))
/ (1.0-ROHW (RAM) * SFWW)
【数3】 (Equation 3)
【0038】ここで、 RHWP(IHEAT,RAM) :IHEATの波長RAMのエネルギが周囲壁
面で反射してPCBに届く割合 ROHW(RAM) : 波長RAMの周囲壁面の反射率 RHWP(IHEAT) :IHEATのエネルギが周囲壁面で反射してPC
Bに届く割合 である。Here, RHWP (IHEAT, RAM) is the ratio of the energy of the wavelength RAM of the IHEAT reflected on the surrounding wall surface and reaches the PCB. ROHW (RAM) is the reflectance of the surrounding wall surface of the wavelength RAM. RHWP (IHEAT): Energy is reflected on the surrounding wall and PC
This is the percentage that reaches B.
【0039】次に、計算要素が受けるエネルギの算出を
実行する。 [1]被加熱体の各材質に対する計算(材質の数だけ計
算) 計算要素は赤外線を透過しないほど十分厚いものとし、
取り扱う計算要素は空気との境界にある要素のみとす
る。 要素がヒータと平行:X=1,垂直:X=0 ヒータに垂直な任意の位置の形態係数は平行な位置の2
5%とする。Next, calculation of the energy received by the calculation element is executed. [1] Calculation for each material of the object to be heated (calculated by the number of materials) The calculation element shall be thick enough not to transmit infrared rays.
Only the elements at the boundary with the air are handled. The element is parallel to the heater: X = 1, vertical: X = 0 The view factor at an arbitrary position perpendicular to the heater is 2 at the parallel position.
5%.
【0040】まず、図7に示す計算要素がヒータから直
接受けるエネルギを次の要領で算出する。 SQHP(IHEAT,RAM) = (X-(X-1) * 0.25) * SFHP(IHEAT)*
EPUP(RAM) * QH(IHEAT,RAM) / APCBFirst, the energy directly received from the heater by the calculation elements shown in FIG. 7 is calculated in the following manner. SQHP (IHEAT, RAM) = (X- (X-1) * 0.25) * SFHP (IHEAT) *
EPUP (RAM) * QH (IHEAT, RAM) / APCB
【数4】 または、 SQHP(IHEAT) = (X-(X-1) * 0.25) * SFHP(IHEAT)* EPUP
* QH(IHEAT) / APCB(Equation 4) Or SQHP (IHEAT) = (X- (X-1) * 0.25) * SFHP (IHEAT) * EPUP
* QH (IHEAT) / APCB
【0041】計算要素がプリント板の基準面より上にあ
る場合(Z>0)When the calculation element is above the reference plane of the printed board (Z> 0)
【数5】 (Equation 5)
【0042】計算要素がプリント板の基準面より下にあ
る場合(Z≦0)When the calculation element is below the reference plane of the printed board (Z ≦ 0)
【数6】 (Equation 6)
【0043】ここで、 SQHP(IHEAT,RAM) :IHEATから計算要素が直接受ける波長
RAMのエネルギ EPUP(RAM) : 計算要素の波長RAMの吸収率 SQHP(IHEAT) :IHEATから計算要素が直接受けるエネルギ EPUP :計算要素の平均吸収率 TSQHP : 上面(又は下面)全てのヒータからPCBが直接
受けるエネルギ である。Here, SQHP (IHEAT, RAM): wavelength directly received by the calculation element from IHEAT
Energy of RAM EPUP (RAM): Wavelength of calculation element Absorption rate of RAM SQHP (IHEAT): Energy directly received by calculation element from IHEAT EPUP: Average absorption rate of calculation element TSQHP: PCB from all upper (or lower) heaters It is the energy directly received.
【0044】次に図8に示す計算要素が周囲壁面から直
接受けるエネルギを次の要領で算出する。 SQWP(RAM) = (X-(X-1) * 0.25) * SFWP* EPUP(RAM) * Q
W(RAM) / (2.0 * APCB)Next, the energy which the calculation element shown in FIG. 8 directly receives from the surrounding wall surface is calculated in the following manner. SQWP (RAM) = (X- (X-1) * 0.25) * SFWP * EPUP (RAM) * Q
W (RAM) / (2.0 * APCB)
【0045】[0045]
【数7】 または、 SQWP = (X-(X-1) * 0.25) * SFWP * EPUP * QW / (2.0*
APCB)(Equation 7) Or SQWP = (X- (X-1) * 0.25) * SFWP * EPUP * QW / (2.0 *
APCB)
【0046】ここで、 SQWP(RAM) : 周囲壁面から計算要素が直接受ける波長RA
Mのエネルギ SQWP :周囲壁面から計算要素が直接受けるエネルギ である。Here, SQWP (RAM) is the wavelength RA directly received by the calculation element from the surrounding wall.
M energy SQWP: Energy directly received by the calculation element from the surrounding wall.
【0047】次に、図9に示す周囲壁面で反射して計算
要素が受けるエネルギを次のように算出する。 SQHWP(IHEAT,RAM) = (X-(X-1) * 0.25) * RHWP(IHEAT)
* EPUP(RAM)* QH(IHEAT,RAM) / (2.0 * APCB)Next, the energy reflected by the peripheral wall surface shown in FIG. 9 and received by the calculation element is calculated as follows. SQHWP (IHEAT, RAM) = (X- (X-1) * 0.25) * RHWP (IHEAT)
* EPUP (RAM) * QH (IHEAT, RAM) / (2.0 * APCB)
【数8】 または、 SQHWP(IHEAT) = (X-(X-1) * 0.25) * RHWP(IHEAT)* EPU
P * QH(IHEAT) / (2.0 * APCB)(Equation 8) Or SQHWP (IHEAT) = (X- (X-1) * 0.25) * RHWP (IHEAT) * EPU
P * QH (IHEAT) / (2.0 * APCB)
【数9】 (Equation 9)
【0048】ここで、 SQHWP(IHEAT,RAM) :壁面で反射して計算要素が受けるIH
EATの波長RAMのエネルギ SQHWP(IHEAT) :壁面で反射して計算要素が受けるIHEAT
のエネルギ TSQHWP :壁面で反射して計算要素が受けるすべてのヒー
タのエネルギ である。Here, SQHWP (IHEAT, RAM): IH reflected on the wall surface and received by the calculation element
EAT wavelength RAM energy SQHWP (IHEAT): IHEAT reflected by the wall and received by the calculation element
Energy TSQHWP: Energy of all heaters reflected by the wall and received by the calculation element.
【0049】次に、図10に示す計算要素が放射により
失うエネルギを次の要領で算出する。 SQP(RAM) = (EPUP(RAM) * C1 * RAM-5)/(exp(C2 / (RAM
* TPCB)) -1)Next, the energy lost by the calculation elements shown in FIG. 10 due to radiation is calculated in the following manner. SQP (RAM) = (EPUP (RAM) * C1 * RAM -5 ) / (exp (C2 / / RAM
* TPCB)) -1)
【数10】 または SQP = EPUP * SIG * TPCB4 (Equation 10) Or SQP = EPUP * SIG * TPCB 4
【0050】ここで、 SQP(RAM) :計算要素が放射する波長RAMのエネルギ TPCB :計算要素の温度 SQP : 計算要素が放射するエネルギ である。Here, SQP (RAM): energy of the wavelength RAM radiated by the calculation element TPCB: temperature of the calculation element SQP: energy radiated by the calculation element.
【0051】次に、図11に示すように計算要素につい
てのエネルギの収支を計算する。 SQ = TSQHP + SQWP + TSQHWP - SQP ここで、 SQ :計算要素が受ける正味のエネルギ である。Next, as shown in FIG. 11, the energy balance of the calculation element is calculated. SQ = TSQHP + SQWP + TSQHWP-SQP where SQ is the net energy received by the computational element.
【0052】以上のふく射計算によって求めた熱量を対
象の計算要素に境界条件として与え被加熱体の熱伝導解
析を行う。また加熱炉内は対流熱伝達による熱量の授受
も無視できない場合が多く、これも考慮すべきことはい
うまでもない。The heat quantity obtained by the above radiation calculation is given to the target calculation element as a boundary condition, and the heat conduction of the object to be heated is analyzed. In the heating furnace, the transfer of heat due to convective heat transfer is often not negligible, and it is needless to say that this should be taken into account.
【0053】この発明では、赤外線ヒータや被加熱体の
材質特有の放射率、吸収率、ふく射エネルギ強度の波長
分布を考慮してふく射伝熱の計算を行うため、赤外線ヒ
ータと被加熱体が持つふく射エネルギ強度の波長分布と
放射率、吸収率の波長分布を赤外線の波長域で複数個に
分割し、それぞれの分割した波長域における被加熱体へ
のふく射熱量の収支を計算し、最後にこれら分割した波
長域における収支を合算する。In the present invention, since the radiation heat transfer is calculated in consideration of the wavelength distribution of the emissivity, absorptance and radiation energy intensity specific to the material of the infrared heater and the object to be heated, the infrared heater and the object to be heated have Divide the wavelength distribution of radiation energy intensity and the wavelength distribution of emissivity and absorptance into a plurality of parts in the infrared wavelength range, calculate the balance of the amount of radiation heat to the object to be heated in each divided wavelength range, and finally calculate these The balance in the divided wavelength range is added.
【0054】このため赤外線ヒータの放射特性に対して
被加熱体が加熱されやすいか否か、赤外線ヒータと被加
熱体のふく射特性のマッチングはどうかといったことを
ふく射計算を行い被加熱体を熱解析した結果に反映する
ことができる。For this reason, a radiation analysis is performed to determine whether the object to be heated is easily heated with respect to the radiation characteristics of the infrared heater, and whether the radiation characteristics of the infrared heater and the object to be heated are matched, and the object to be heated is thermally analyzed. Can be reflected in the results.
【0055】また、赤外線加熱炉内の被加熱体の温度を
検出するための被加熱体の熱解析において、被加熱体が
受けるふく射熱量の計算に、被加熱体、赤外線ヒータ、
周囲壁面などとの間の形態係数と、この時間変化を考慮
するため、解析のタイムステップ毎あるいは複数のタイ
ムステップ毎に各形態係数を計算し、これを用いてヒー
タから被加熱体が受けるふく射熱量を計算し、これと被
加熱体自身が放射するふく射熱量との収支計算を行なっ
たあと、これを境界条件として被加熱体の熱伝導解析を
行い、温度分布やこの時間変化を知る。Further, in the thermal analysis of the object to be heated for detecting the temperature of the object to be heated in the infrared heating furnace, the amount of radiant heat received by the object to be heated is calculated by using the object to be heated, the infrared heater,
In order to consider the view factor between the surrounding wall and the like, and this time change, calculate each view factor for each analysis time step or for each of a plurality of time steps, and use this to calculate the radiation heat received by the heater from the heater using the heater. After calculating the amount and calculating the balance of the amount of radiation and the amount of radiation heat radiated by the heated object itself, the heat conduction analysis of the heated object is performed using this as a boundary condition to know the temperature distribution and its time change.
【0056】このため、各ヒータと被加熱体との相対的
な位置関係に応じたふく射エネルギの時間変化を正確に
計算することが出来る。このように、熱伝導解析を行う
対象に境界条件として設定する、ふく射熱量とこの時間
変化を正確に計算できるため、定量的に正確な解析結果
を得ることができ、被加熱体の正確な温度検知が可能と
なり、これを利用することにより、実際にプリント板の
加熱実験を行うことなく、効率よく赤外線リフロー炉の
加熱条件の設定を行うことが出来る。For this reason, it is possible to accurately calculate the time change of the radiation energy according to the relative positional relationship between each heater and the object to be heated. In this way, since the amount of radiated heat and its time change, which are set as boundary conditions for the object to be subjected to heat conduction analysis, can be calculated accurately, a quantitatively accurate analysis result can be obtained, and the accurate temperature of the object to be heated can be obtained. The detection can be performed, and by using this, the heating conditions of the infrared reflow furnace can be set efficiently without actually performing the heating experiment of the printed board.
【0057】この技術は赤外線リフロー炉内のプリント
配線板の温度検知や赤外線リフロー炉の加熱条件の設定
に利用するのみでなく、例えば塗装の乾燥食品の加工な
どに使用される加熱装置内の被加熱体の温度検知や加熱
装置の加熱条件の設定にも適用できる。This technique is used not only for detecting the temperature of the printed wiring board in the infrared reflow furnace and setting the heating conditions of the infrared reflow furnace, but also for controlling the temperature of the printed circuit board in a heating device used for processing, for example, a dried food product. The present invention is also applicable to temperature detection of a heating element and setting of heating conditions of a heating device.
【0058】実施例 以下にこの発明の実施例を詳述する。Embodiments Embodiments of the present invention will be described below in detail.
【0059】図12に示す赤外線リフロー炉を用いて、
図13に示すプリント板Pを加熱した場合のプリント板
の非定常熱伝導解析を行った。なお、基板Pには図13
に示すようにコンデンサC、QFP(Quad Flat Packag
e)型集積素子IC1、SOP(Small Outline Package)
型集積素子IC2およびコネクタSが搭載されているも
のとする。図12において赤外線リフロー炉は、予熱ゾ
ーン5、均熱ゾーン6、本加熱ゾーン8、及びプリント
板Pを矢印方向に搬送するコンベア7などによって構成
されている。プリント板Pを搬送するコンベア7の上下
には予熱ゾーン5、均熱ゾーン6および、本加熱ゾーン
8に対応し面状の赤外線ヒータHが搬送方向に沿って所
定の間隔で上下に設置されている。Using an infrared reflow furnace shown in FIG.
Unsteady heat conduction analysis of the printed board P when the printed board P shown in FIG. 13 was heated was performed. It should be noted that the substrate P
Capacitor C and QFP (Quad Flat Packag)
e) type integrated device IC1, SOP (Small Outline Package)
It is assumed that the integrated device IC2 and the connector S are mounted. In FIG. 12, the infrared reflow furnace is constituted by a preheating zone 5, a soaking zone 6, a main heating zone 8, a conveyor 7 for transporting the printed board P in the direction of the arrow, and the like. Above and below the conveyer 7 for transporting the printed board P, planar heaters H corresponding to the preheating zone 5, the soaking zone 6 and the main heating zone 8 are provided at predetermined intervals along the transport direction. I have.
【0060】ヒータにより各ゾーンは異なる温度に保た
れており、予熱ゾーン5は340℃、均熱ゾーン6は1
70℃、均熱ゾーン7は170℃、本加熱ゾーン8は3
60℃となっているため、各ヒータHからプリント板P
が受けるふく射エネルギを各々計算するようにした。Each zone is maintained at a different temperature by a heater, the preheating zone 5 is 340 ° C., and the soaking zone 6 is 1
70 ° C, soaking zone 7 is 170 ° C, main heating zone 8 is 3
Since the temperature is 60 ° C., the printed board P
The radiation energy received by each was calculated.
【0061】更に、周囲壁面が放射するふく射エネルギ
と、各赤外線ヒータから周囲壁面に反射してプリント板
Pに届くふく射エネルギと、プリント板Pから周囲空間
へのふく射エネルギを各々計算し、これらの収支計算を
行った。Further, the radiation energy radiated from the peripheral wall surface, the radiation energy reflected from each infrared heater to the peripheral wall surface and reaching the printed board P, and the radiation energy from the printed board P to the surrounding space are calculated. A balance calculation was performed.
【0062】また、このふく射エネルギの収支計算は2
〜27μmの波長の間を1μm間隔で分割し、各々の波
長範囲毎に行った。赤外線ヒータHからプリント板Pへ
のふく射エネルギの計算において、赤外線ヒータHから
プリント板Pへの形態係数は、今回、解析したプリント
板PはヒータHと比べて小さいため、プリント板P上の
位置の違いによるヒータHからの形態係数の違いが微小
であるため、プリント板P上の任意の位置で一定と仮定
した。また赤外線ヒータHからヒータに垂直な面への形
態係数は、改めて計算せずに赤外線ヒータHから水平な
面への形態係数の1/4とした。The calculation of the radiation energy balance is 2
The wavelength of ~ 27 μm was divided at 1 μm intervals, and the measurement was performed for each wavelength range. In the calculation of the radiation energy from the infrared heater H to the printed board P, the view factor from the infrared heater H to the printed board P was smaller than that of the heater H analyzed this time. Since the difference in the form factor from the heater H due to the difference is small, it is assumed that the difference is constant at an arbitrary position on the printed board P. Further, the view factor from the infrared heater H to the plane perpendicular to the heater was set to 1 / of the view factor from the infrared heater H to the horizontal plane without being calculated again.
【0063】これらの形態係数およびふく射エネルギの
計算は、プリント板Pがリフロー炉内をコンベア7によ
って移動し、時間によって変化するため、熱伝導解析の
各タイムステップ毎に計算するようにした。更にリフロ
ー炉内の雰囲気とプリント板Pと対流熱伝達による熱交
換に関しては、ここでは簡単に熱伝達係数を一定とし、
プリント板Pの上面、下面とも10W/m2Kとし、炉内雰
囲気の温度を140℃(測定値)一定として計算した。The calculation of the form factor and the radiation energy is performed at each time step of the heat conduction analysis because the printed board P moves in the reflow furnace by the conveyor 7 and changes with time. Further, regarding heat exchange by convection heat transfer with the atmosphere in the reflow furnace and the printed board P, here, the heat transfer coefficient is simply fixed,
The calculation was performed with the upper surface and the lower surface of the printed board P being 10 W / m 2 K and the temperature of the furnace atmosphere being constant at 140 ° C. (measured value).
【0064】以上の計算から各タイムステップにおける
プリント板P上の各境界要素に対する境界条件を決定
し、リフロー炉入口から出口まで(180秒間)移動す
るプリント板Pの180秒間の非定常熱伝導解析を行っ
た。熱伝導解析手法として三次元差分法を用いた。From the above calculations, the boundary conditions for each boundary element on the printed board P at each time step are determined, and the transient heat conduction analysis of the printed board P moving from the inlet to the outlet of the reflow furnace (180 seconds) for 180 seconds. Was done. A three-dimensional difference method was used as a heat conduction analysis method.
【0065】また、この実施例においては、解析結果の
定量的な正確さを証明するため、リフロー炉で熱電対を
設置したプリント板Pを加熱し、温度プロファイルを実
測する実験を行った。測定点は図13に示す点a、bで
ある。In this example, in order to prove the quantitative accuracy of the analysis result, an experiment was conducted in which the printed board P on which a thermocouple was installed was heated by a reflow furnace and the temperature profile was measured. The measurement points are points a and b shown in FIG.
【0066】図14および図15にこの実施例による解
析結果の温度プロファイル(イ)と実験結果の温度プロ
ファイル(ロ)をそれぞれ示す。図14は、図13に示
すプリント板Pの電子部品が搭載されていない点aの温
度、図15は図13に示す電子部品が搭載されている点
bの温度である。これよりこの実施例による解析結果の
描く温度プロファイル(イ)は、QFP型集積回路など
比較的大きな電子部品の下の基板の温度が、搭載されて
いない部分の基板の温度と比較して低くなり、実験結果
の描く温度プロファイルの曲線(ロ)と相似関係にある
など定性的に正しいことが確認された。FIGS. 14 and 15 show a temperature profile (a) of the analysis result and a temperature profile (b) of the experimental result according to this embodiment, respectively. 14 shows the temperature at point a where the electronic component of the printed board P shown in FIG. 13 is not mounted, and FIG. 15 shows the temperature at point b where the electronic component shown in FIG. 13 is mounted. Accordingly, the temperature profile (a) drawn by the analysis result according to this embodiment is such that the temperature of the substrate under a relatively large electronic component such as a QFP type integrated circuit is lower than the temperature of the substrate not mounted on the substrate. It was confirmed qualitatively correct that it had a similar relationship with the temperature profile curve (b) drawn by the experimental results.
【0067】また、表1に図13の点aにおけるこの実
施例の方法による解析結果と実験による温度測定の結果
を定量的に比較した。表2に図3の点bにおけるこの実
施例の方法による解析結果と実験による温度測定の結果
を定量的に比較した。この発明の解析手法を用いた結果
は、実験結果と比べて点aに関しては、190℃(22
→212℃)の温度上昇に対して−3〜+4℃以内、±
2.1%以内の誤差であり、点bに関しては、168℃
(22→190℃)の温度上昇に対して−5〜+5℃以
内、、±3%以内の誤差である。Table 1 quantitatively compares the results of the analysis at the point a in FIG. 13 by the method of this embodiment with the results of the temperature measurement by experiment. Table 2 quantitatively compares the results of the analysis at the point b in FIG. 3 by the method of this example with the results of the temperature measurement by experiment. The results obtained by using the analysis method of the present invention are as follows.
→ 212 ° C) within -3 to + 4 ° C, ±
Error within 2.1%, 168 ° C. for point b
The error is within -5 to + 5 ° C and within ± 3% for the temperature rise of (22 → 190 ° C).
【0068】以上の結果から、この発明の方法によれ
ば、高い精度でプリント板の温度を検知できる。またこ
の検知方法を用いることで、実際にプリント板をリフロ
ー炉で加熱し熱電対などを用いて温度を測定することな
く、リフロー炉のヒータ温度等の加熱条件を効率よく設
定することが可能である。From the above results, according to the method of the present invention, the temperature of the printed board can be detected with high accuracy. By using this detection method, it is possible to efficiently set the heating conditions such as the heater temperature of the reflow furnace without actually heating the printed board in a reflow furnace and measuring the temperature using a thermocouple or the like. is there.
【0069】[0069]
【表1】 [Table 1]
【0070】[0070]
【表2】 [Table 2]
【0071】[0071]
【発明の効果】この発明によれば、赤外線リフロー炉内
のプリント板の熱解析において、プリント板およびプリ
ント板上の電子部品が受けるふく射熱量の計算に、被加
熱体、赤外線ヒータ、炉内壁面などの間の形態係数を考
慮するため、従来のふく射計算方法を用いた解析方法に
比べて被加熱体の温度分布やこの時間変化など、定量的
に精度のよい解析結果を得ることができる。According to the present invention, in the thermal analysis of a printed circuit board in an infrared reflow furnace, the calculation of the amount of radiant heat received by the printed circuit board and the electronic components on the printed circuit board can be performed by using the object to be heated, the infrared heater, and the furnace inner wall surface. In consideration of the view factor during the time, for example, it is possible to obtain a quantitatively accurate analysis result such as the temperature distribution of the object to be heated and its time change as compared with an analysis method using a conventional radiation calculation method.
【0072】更に解析結果の定量的な信頼性が高いた
め、解析を多くても数回実行するのみで、赤外線ヒータ
の温度およびコンベア速度の最適な設定を行える。この
ため従来の様に作業者の勘や経験に頼ることなく被加熱
体の最適な温度プロファイルを得ることができ、更には
実際に赤外線加熱炉に被加熱体を通して温度分布を測定
するなど補助的な実験が必要でないため、作業性がよく
加熱炉の設備稼働率を向上させることが可能となる。Further, since the analysis result has high quantitative reliability, the temperature of the infrared heater and the conveyor speed can be set optimally by executing the analysis at most several times. For this reason, it is possible to obtain the optimum temperature profile of the object to be heated without relying on the intuition and experience of the operator as in the past, and to actually measure the temperature distribution through the object through the infrared heating furnace. Since a simple experiment is not required, workability is good and the equipment operation rate of the heating furnace can be improved.
【図1】この発明の計算方法に用いる赤外線加熱炉の構
成説明図である。FIG. 1 is a diagram illustrating the configuration of an infrared heating furnace used in a calculation method according to the present invention.
【図2】この発明の計算過程の概要を示すフローチャー
トである。FIG. 2 is a flowchart showing an outline of a calculation process according to the present invention.
【図3】この発明の計算過程の要部を示すフローチャー
トである。FIG. 3 is a flowchart showing a main part of a calculation process according to the present invention.
【図4】この発明の計算過程の要部を示すフローチャー
トである。FIG. 4 is a flowchart showing a main part of a calculation process according to the present invention.
【図5】この発明の計算過程の要部を示すフローチャー
トである。FIG. 5 is a flowchart showing a main part of a calculation process according to the present invention.
【図6】この発明の計算過程の要部を示すフローチャー
トである。FIG. 6 is a flowchart showing a main part of a calculation process according to the present invention.
【図7】この発明の計算過程の要部を示すフローチャー
トである。FIG. 7 is a flowchart showing a main part of a calculation process according to the present invention.
【図8】この発明の計算過程の要部を示すフローチャー
トである。FIG. 8 is a flowchart showing a main part of a calculation process according to the present invention.
【図9】この発明の計算過程の要部を示すフローチャー
トである。FIG. 9 is a flowchart showing a main part of a calculation process according to the present invention.
【図10】この発明の計算過程の要部を示すフローチャ
ートである。FIG. 10 is a flowchart showing a main part of a calculation process according to the present invention.
【図11】この発明の計算過程の要部を示すフローチャ
ートである。FIG. 11 is a flowchart showing a main part of a calculation process according to the present invention.
【図12】この発明の実施例に用いる赤外線リフロー炉
の構成説明図である。FIG. 12 is a configuration explanatory view of an infrared reflow furnace used in an embodiment of the present invention.
【図13】この発明の実施例に用いるプリント板の上面
図である。FIG. 13 is a top view of a printed board used in the embodiment of the present invention.
【図14】この発明の実施例による算出値と実験による
実測値との温度プロファイル図である。FIG. 14 is a temperature profile diagram of a calculated value according to the embodiment of the present invention and an actually measured value according to an experiment.
【図15】この発明の実施例による算出値と実験による
実測値との温度プロファイル図である。FIG. 15 is a temperature profile diagram of a calculated value according to the embodiment of the present invention and an actually measured value according to an experiment.
Claims (5)
体の温度を数値解析によって検知する際に、赤外線の波
長域を複数の範囲に分割し、それぞれの分割した波長域
毎に、被加熱体がヒータから受けるふく射熱量と周囲に
放射するふく射熱量との収支を計算し、これらを合算し
て被加熱体が炉内で受ける正味のふく射熱量を計算し、
これを境界条件として被加熱体の熱解析を行い、被加熱
体の温度を検知することを特徴とする赤外線加熱炉内の
被加熱体の温度検知方法。When detecting the temperature of an object to be heated in a heating furnace having an infrared heater by numerical analysis, an infrared wavelength range is divided into a plurality of ranges, and each of the divided wavelength ranges is heated. Calculate the balance between the amount of radiant heat received by the body from the heater and the amount of radiant heat radiated to the surroundings, add these together to calculate the net radiant heat received by the heated body in the furnace,
A method for detecting the temperature of a heated object in an infrared heating furnace, wherein the temperature of the heated object is detected by performing a thermal analysis of the heated object using the boundary conditions as a boundary condition.
と周囲に放射するふく射熱量との収支を計算する工程
が、赤外線ヒータと被加熱体との間の形態係数を計算
し、これを用いてふく射熱量の収支計算を行うことを特
徴とする請求項1記載の赤外線加熱炉内の被加熱体の温
度検知方法。2. The step of calculating the balance between the amount of radiant heat received by the object to be heated from the heater and the amount of radiant heat radiated to the surroundings includes calculating a view factor between the infrared heater and the object to be heated, and using the same. 2. The method for detecting the temperature of an object to be heated in an infrared heating furnace according to claim 1, wherein the calculation of the amount of radiation heat is performed.
体の温度を数値解析によって検知する際に、加熱炉内で
の被加熱体の相対的な位置が時間によって変化する場
合、赤外線ヒータと被加熱体との間の形態係数を、時間
の関数として計算し、これを用いて被加熱体が炉内で受
ける正味のふく射熱量を計算し、これを境界条件として
被加熱体の熱解析を行い、被加熱体の温度を検知するこ
とを特徴とする赤外線加熱炉内の被加熱体の温度検知方
法。3. When detecting the temperature of a heated object in a heating furnace having an infrared heater by numerical analysis, when the relative position of the heated object in the heating furnace changes over time, Calculate the view factor between the object and the object as a function of time, use this to calculate the net radiant heat received by the object in the furnace, and use this as the boundary condition for thermal analysis of the object. And detecting the temperature of the object to be heated in the infrared heating furnace.
請求項3に記載の方法とを合わせて用い、被加熱体が炉
内で受ける正味のふく射熱量を計算し、これを境界条件
とし被加熱体の熱解析を行い、被加熱体の温度分布や温
度上昇を検知することを特徴とする赤外線加熱炉内の被
加熱体の温度検知方法。4. The method according to claim 1 and the method according to claim 2 or 3 are used together to calculate a net radiant heat received by the object to be heated in the furnace, and calculate this as a boundary condition. A method for detecting a temperature of a heated object in an infrared heating furnace, wherein a temperature distribution and a temperature rise of the heated object are detected by performing a thermal analysis of the heated object.
量の計算において、被加熱体が赤外線ヒータから直接受
けるふく射熱量の他に、炉内壁面からのふく射熱量と、
赤外線ヒータから炉内壁面に反射して被加熱体に届くふ
く射熱量とを考慮して、ふく射熱量の収支計算を行うこ
とを特徴とする請求項1〜4のいずれかに記載の赤外線
加熱炉内の被加熱体の温度検知方法。5. The calculation of the net radiant heat received by the object in the furnace, in addition to the amount of radiant heat received by the object directly from the infrared heater,
The infrared heating furnace according to any one of claims 1 to 4, wherein the calculation of the amount of radiation heat is performed in consideration of the amount of radiation heat reflected from the infrared heater to the furnace inner wall and reaching the object to be heated. Temperature detection method of the object to be heated.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15237796A JPH102801A (en) | 1996-06-13 | 1996-06-13 | Temperature detection method of the object to be heated in infrared heating furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15237796A JPH102801A (en) | 1996-06-13 | 1996-06-13 | Temperature detection method of the object to be heated in infrared heating furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH102801A true JPH102801A (en) | 1998-01-06 |
Family
ID=15539203
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15237796A Pending JPH102801A (en) | 1996-06-13 | 1996-06-13 | Temperature detection method of the object to be heated in infrared heating furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH102801A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2001050356A1 (en) * | 2000-01-04 | 2001-07-12 | Fujitsu Limited | Method and apparatus for designing printed-circuit board |
| WO2002075264A1 (en) * | 2001-03-06 | 2002-09-26 | Tokyo Electron Limited | Temperature measuring method and apparatus and semiconductor heat treatment apparatus |
| CN116149391A (en) * | 2022-12-20 | 2023-05-23 | 江苏电子信息职业学院 | Furnace temperature curve control method based on one-dimensional unsteady state heat conduction model |
-
1996
- 1996-06-13 JP JP15237796A patent/JPH102801A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2001050356A1 (en) * | 2000-01-04 | 2001-07-12 | Fujitsu Limited | Method and apparatus for designing printed-circuit board |
| US6662345B2 (en) | 2000-01-04 | 2003-12-09 | Fujitsu Limited | Method and apparatus for designing printed-circuit board |
| WO2002075264A1 (en) * | 2001-03-06 | 2002-09-26 | Tokyo Electron Limited | Temperature measuring method and apparatus and semiconductor heat treatment apparatus |
| CN116149391A (en) * | 2022-12-20 | 2023-05-23 | 江苏电子信息职业学院 | Furnace temperature curve control method based on one-dimensional unsteady state heat conduction model |
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