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JP2018105516A - Paint drying equipment - Google Patents

Paint drying equipment Download PDF

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JP2018105516A
JP2018105516A JP2016249304A JP2016249304A JP2018105516A JP 2018105516 A JP2018105516 A JP 2018105516A JP 2016249304 A JP2016249304 A JP 2016249304A JP 2016249304 A JP2016249304 A JP 2016249304A JP 2018105516 A JP2018105516 A JP 2018105516A
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furnace
temperature furnace
path
exhaust
temperature
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JP6741568B2 (en
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小林 孝次
Koji Kobayashi
孝次 小林
清一 石関
Seiichi Ishizeki
清一 石関
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Subaru Corp
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Subaru Corp
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

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  • Drying Of Solid Materials (AREA)
  • Coating Apparatus (AREA)
  • Tunnel Furnaces (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Furnace Details (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide coating drying equipment where, even in the case exhaust heat from a high temperature furnace is fed to a low temperature furnace, the furnace temperature of the low temperature furnace can be easily regulated.SOLUTION: Hot wind heated by a heating furnace 22 is fed to a high temperature furnace 15 to heat the inside of the furnace, exhaust gas after the heating is purified by a filter box 25 and is fed to a low temperature furnace 16. External air is freely introduced into the filter box 25 via a second damper 34, and, by the opening degree of the second damper 34, the flow rate of the external air to be introduced into the filter box 25 is controlled, and it is mixed with exhaust has to regulate the quantity of the hot wind to be fed into the low temperature furnace 16.SELECTED DRAWING: Figure 3

Description

本発明は、高温炉内を加熱した熱風の排気で低温炉内を加熱するようにした塗装乾燥設備に関する。   The present invention relates to a coating drying facility in which the inside of a low-temperature furnace is heated by exhaust of hot air heated in the high-temperature furnace.

自動車等の車体を構成する主要部品は、金属材料が多く採用されているが、車体の軽量化、デザイン性等の観点から、車体本体に取付ける周辺部品を、従来の金属製部品から樹脂製部品に切換える傾向にある。   The main parts that make up the body of automobiles, etc., are often made of metal materials. However, from the viewpoints of weight reduction and design, etc., peripheral parts to be mounted on the body of the car body are changed from conventional metal parts to resin parts. Tend to switch to

この場合、金属製部品と樹脂製部品とを同一の乾燥焼付炉で乾燥焼付けを行った場合、耐熱温度の相違から、樹脂材料が熱変形する可能性があるため、両部品を別々の乾燥焼付炉で行う必要がある。   In this case, if the metal parts and the resin parts are dry-baked in the same dry-baking furnace, the resin material may be thermally deformed due to the difference in heat-resistant temperature. Must be done in a furnace.

例えば特許文献1(特公昭58−3191号公報)には、高温乾燥焼付炉(高温炉)からの排気を直接、或いはアフターバーナ及び触媒を通過させて浄化した後、低温乾燥焼付炉(低温炉)へ供給することで熱エネルギを有効活用するようにした技術が開示されている。   For example, in Patent Document 1 (Japanese Patent Publication No. 58-3191), exhaust from a high temperature drying baking furnace (high temperature furnace) is purified directly or after passing through an afterburner and a catalyst, and then a low temperature drying baking furnace (low temperature furnace). ) Has been disclosed in which thermal energy is effectively utilized by supplying to (1).

特公昭58−3191号公報Japanese Patent Publication No.58-3191

上述した文献に開示されている技術では、高温炉からの排気熱を低温炉に供給するようにしているため、低温炉の炉内温度は高温炉側から供給される排気熱で決定されてしまうことになる。   In the technique disclosed in the above-described document, the exhaust heat from the high temperature furnace is supplied to the low temperature furnace, so the temperature inside the low temperature furnace is determined by the exhaust heat supplied from the high temperature furnace side. It will be.

しかし、低温炉での樹脂製部品に対する乾燥焼付け温度範囲は予め決められており、この乾燥焼付温度に対して、高温炉から供給される排気熱温度が高い場合、温度調整することができず、所定乾燥後の樹脂製部品の色相と金属製部品の色相との差(色差)が大きくなり易い。その結果、塗装完了後の色相調整に要する負担が増加して生産効率の低下を招く不都合がある。   However, the dry baking temperature range for resin parts in a low temperature furnace is predetermined, and if the exhaust heat temperature supplied from the high temperature furnace is high relative to this dry baking temperature, the temperature cannot be adjusted, The difference (color difference) between the hue of the resin part after predetermined drying and the hue of the metal part tends to be large. As a result, there is an inconvenience that the burden required for the hue adjustment after the completion of painting is increased and the production efficiency is lowered.

本発明は、上記事情に鑑み、高温炉からの排気熱を低温炉に供給する場合であっても、低温炉の炉内温度を容易に調整することができ、塗装完了後の色相調整に要する負担を大幅に軽減して、生産効率の向上を図ることのできる塗装乾燥設備を提供することを目的とする。   In view of the above circumstances, the present invention can easily adjust the temperature in the furnace of the low-temperature furnace even when the exhaust heat from the high-temperature furnace is supplied to the low-temperature furnace, and is required for hue adjustment after the completion of painting. An object of the present invention is to provide a paint drying facility that can greatly reduce the burden and improve the production efficiency.

本発明は、塗料を塗布した後の金属製部品を乾燥焼付けする高温炉と、塗料を塗布した後の樹脂製部品を乾燥焼付けする低温炉と、前記高温炉に熱風を供給する加熱炉と、前記高温炉を加熱した前記熱風を排出する第1排気路と、前記第1排気路からの排気を前記低温炉に供給する循環路と、前記低温炉からの排気を前記加熱炉へ循環させる第2排気路とを有する塗装乾燥設備において、前記第1排気路と前記循環路とが接続される混合ボックスと、前記混合ボックスに接続された外気導入路と、前記外気導入路に介装されて前記混合ボックスに導入する外気流量を調整する外気流量調整手段と、前記循環路を通過する熱風の熱量を計測する熱量計測手段と、前記熱量計測手段で計測した熱量と予め設定されている前記低温炉内の目標炉温とに基づき前記外気流量調整手段の流量を制御して前記循環路を通過する熱風の熱量を調整する炉内温度制御手段とを更に備える。   The present invention includes a high-temperature furnace for drying and baking metal parts after applying a paint, a low-temperature furnace for drying and baking resin parts after applying a paint, a heating furnace for supplying hot air to the high-temperature furnace, A first exhaust passage for discharging the hot air that has heated the high-temperature furnace, a circulation passage for supplying the exhaust from the first exhaust passage to the low-temperature furnace, and a first circulation for circulating the exhaust from the low-temperature furnace to the heating furnace. In the paint drying facility having two exhaust paths, the mixing box to which the first exhaust path and the circulation path are connected, the outside air introduction path connected to the mixing box, and the outside air introduction path are interposed. An outside air flow rate adjusting means for adjusting the outside air flow rate introduced into the mixing box, a heat amount measuring means for measuring the amount of heat of hot air passing through the circulation path, a heat amount measured by the heat amount measuring means, and the preset low temperature The target furnace temperature in the furnace and Based further comprising a furnace temperature control means for adjusting the amount of heat of the hot by controlling the flow rate through the circulation path of the ambient air flow rate adjusting means.

本発明によれば、炉内温度制御手段によって混合ボックスに導入する外気流量を制御し、低温炉内を加熱する熱風の熱量を制御するようにしたので、高温炉からの排気熱を低温炉に供給する場合であっても、低温炉の炉内温度を容易に調整することができる。その結果、高温炉の金属製部品と低温炉の樹脂製部品とに対して同一の塗料が塗布されている場合であっても、所定に乾燥した後の色差が小さくなり、色相調整に要する負担を大幅に軽減して、生産効率の向上を図ることができる。   According to the present invention, the flow rate of the hot air that heats the inside of the low-temperature furnace is controlled by controlling the flow rate of the outside air introduced into the mixing box by the furnace temperature control means, so that the exhaust heat from the high-temperature furnace is transferred to the low-temperature furnace. Even in the case of supplying, the in-furnace temperature of the low-temperature furnace can be easily adjusted. As a result, even if the same paint is applied to the metal parts of the high temperature furnace and the resin parts of the low temperature furnace, the color difference after predetermined drying is reduced, and the burden required for hue adjustment Can be greatly reduced and production efficiency can be improved.

第1実施形態による塗装乾燥設備の概略構成図Schematic configuration diagram of paint drying equipment according to the first embodiment 同、高温乾燥焼付炉と低温乾燥焼付炉とに対する熱源供給系統を示す概略平面図Schematic plan view showing the heat source supply system for the high-temperature drying baking furnace and the low-temperature drying baking furnace 同、高温乾燥焼付炉と低温乾燥焼付炉とに対する熱源供給系統を示す構成図The same configuration diagram showing the heat source supply system for the high temperature drying baking furnace and the low temperature drying baking furnace 同、図2の熱源供給系統を簡略化した模式図The simplified schematic diagram of the heat source supply system of FIG. 同、炉内温度制御ユニットの構成図Same configuration diagram of furnace temperature control unit 同、高温乾燥焼付炉内温度制御ルーチンを示すフローチャートSame as above, high-temperature drying baking furnace temperature control routine 同、低温乾燥焼付炉内温度制御ルーチンを示すフローチャートSame as above, low temperature drying baking furnace temperature control routine 本発明の第2実施形態による塗装乾燥ラインを示す概略説明図Schematic explanatory drawing which shows the coating drying line by 2nd Embodiment of this invention. 同、塗装乾燥設備の熱源供給系統を示す断面図Sectional view showing the heat source supply system of the paint drying equipment 本発明の第3実施形態による図8相当の概略説明図Schematic explanatory diagram corresponding to FIG. 8 according to a third embodiment of the present invention

以下、図面に基づいて本発明の一実施形態を説明する。   Hereinafter, an embodiment of the present invention will be described with reference to the drawings.

[第1実施形態]
図1〜図7に本発明の第1実施形態を示す。図1に示す塗装設備1は、被塗装部品としての車体M1を構成する金属製部品の一例としての車体本体2と、この車体本体2に取付けられる樹脂製部品の一例としてのフロントバンパ3及びリヤバンパ4に対して同一塗料を塗布し、塗布後の車体本体2とバンパ3,4とを並行して別々に乾燥焼付けするものである。
[First Embodiment]
1 to 7 show a first embodiment of the present invention. A painting facility 1 shown in FIG. 1 includes a vehicle body 2 as an example of a metal part constituting a vehicle body M1 as a part to be painted, and a front bumper 3 and a rear bumper as examples of resin parts attached to the vehicle body 2. 4, the same paint is applied, and the applied body 2 and the bumpers 3 and 4 are separately dried and baked in parallel.

この塗装設備1は、前工程から搬送治具Jt1,Jt2(図3参照)に載置され、コンベヤにて搬送されてきた車体本体2とバンパ3,4とからなる車体M1に対して同一塗料を一括塗布する塗布工程12と、分離乾燥焼付工程13とを備えている。   This coating equipment 1 is placed on the conveying jigs Jt1 and Jt2 (see FIG. 3) from the previous process, and the same paint is applied to the vehicle body M1 composed of the vehicle body 2 and the bumpers 3 and 4 which are conveyed by the conveyor. Are applied at once, and a separation drying baking process 13 is provided.

分離乾燥焼付工程13は、塗布工程12で車体本体2とバンパ3,4とに塗布された塗料を乾燥焼付けするものであり、車体分離部14と高温乾燥焼付炉(以下、「高温炉」と略称)15と低温乾燥焼付炉(以下、「低温炉」と略称)16と色相照合部17と色相調整部18と車体集成部19とを有している。車体分離部14は塗布工程12から搬送されてきた車体M1を車体本体2とバンパ3,4とに、それぞれが載置されている搬送治具Jt1,Jt2を移動させて分離する。   The separation drying baking process 13 is a process for drying and baking the paint applied to the vehicle body 2 and the bumpers 3 and 4 in the coating process 12, and includes a vehicle separation unit 14 and a high temperature drying baking furnace (hereinafter referred to as "high temperature furnace"). (Abbreviation) 15, a low-temperature drying baking furnace (hereinafter abbreviated as “low-temperature furnace”) 16, a hue collation unit 17, a hue adjustment unit 18, and a vehicle body assembly unit 19. The vehicle body separation unit 14 separates the vehicle body M1 conveyed from the coating process 12 by moving the conveyance jigs Jt1 and Jt2 on which the vehicle body M1 is mounted on the vehicle body 2 and the bumpers 3 and 4, respectively.

高温炉15は搬入された金属製の車体本体2を、高温(例えば170°)で予め設定した時間だけ乾燥焼き付けする。又、低温炉16は搬入された樹脂製のバンパ3,4を、高温炉15よりも低い温度(例えば120°)で予め設定した時間だけ乾燥焼き付けする。   The high-temperature furnace 15 dry-bakes the metal body body 2 that has been carried in at a high temperature (for example, 170 °) for a preset time. The low-temperature furnace 16 dry-bakes the loaded resin bumpers 3 and 4 at a temperature (for example, 120 °) lower than that of the high-temperature furnace 15 for a preset time.

色相照合部17は乾燥焼付けの完了した車体本体2とバンパ3,4との色相(Lab値)を比較し、その差(色差)が許容範囲に収まっているか否かを調べる。又、色相調整部18は、色差が許容範囲から外れている場合、その色差が許容範囲に収まるように車体本体2或いはバンパ3,4の色相を調整する。従って、色差が許容範囲に収まっている場合は、車体本体2とバンパ3,4とは、色相調整部18をそのまま通過する。   The hue matching unit 17 compares the hues (Lab values) of the vehicle body 2 and the bumpers 3 and 4 that have been dry-baked, and checks whether the difference (color difference) is within an allowable range. Further, when the color difference is out of the allowable range, the hue adjusting unit 18 adjusts the hue of the vehicle body 2 or the bumpers 3 and 4 so that the color difference is within the allowable range. Accordingly, when the color difference is within the allowable range, the vehicle body 2 and the bumpers 3 and 4 pass through the hue adjusting unit 18 as they are.

又、車体集成部19は、色相調整部18から搬送されてきた車体本体2にバンパ3,4を取付けて車体M1を集成する。そして、この集成された車体M1を後工程(擬装工程)へ搬出させる。   In addition, the vehicle body assembly unit 19 attaches bumpers 3 and 4 to the vehicle body 2 that has been conveyed from the hue adjustment unit 18 to collect the vehicle body M1. Then, the assembled vehicle body M1 is carried out to a subsequent process (imitation process).

図2に示すように、高温炉15と低温炉16とは、車体本体2とバンパ3,4とを一定速度で移動させる際に乾燥焼き付けするための所定ライン長を有しており、図3に示すように、高温炉15と低温炉16との両側下部に、熱風導入口15a,16aが炉長に沿って所定間隔を開けて開口されている。又、この熱風導入口15a,16aの上方に排気口15b,16bが炉長に沿って所定間隔を開けて開口されている。   As shown in FIG. 2, the high temperature furnace 15 and the low temperature furnace 16 have a predetermined line length for drying and baking when the vehicle body 2 and the bumpers 3 and 4 are moved at a constant speed. As shown in FIG. 2, hot air inlets 15a, 16a are opened at predetermined intervals along the length of the furnace at both lower portions of the high-temperature furnace 15 and the low-temperature furnace 16. Exhaust ports 15b and 16b are opened above the hot air inlets 15a and 16a at predetermined intervals along the furnace length.

高温炉15に開口されている各熱風導入口15aに、第1送気路としての第1送気ダクト21の分岐された下流端がそれぞれ接続され、この第1送気ダクト21の集合された上流側が加熱炉22に接続されている。又、この第1送気ダクト21の集合部分に、熱風を熱風導入口の方向へ送気する第1送風ファン23が介装されている。   The branched downstream ends of the first air supply duct 21 serving as the first air supply path are respectively connected to the hot air inlets 15a opened in the high temperature furnace 15, and the first air supply duct 21 is assembled. The upstream side is connected to the heating furnace 22. In addition, a first blower fan 23 that supplies hot air in the direction of the hot air introduction port is interposed in the assembly portion of the first air supply duct 21.

又、高温炉15に開口されている排気口15bに第1排気路としての第1排気ダクト24の上流端が接続されており、この第1排気ダクト24の下流側が集合されてフィルタボックス25に接続され、この集合部分に排気をフィルタボックス25の方向へ送気する第2送風ファン26が介装されている。尚、フィルタボックス25は高温炉15から排出された排気を浄化するものである。   An upstream end of a first exhaust duct 24 serving as a first exhaust path is connected to an exhaust port 15 b opened in the high-temperature furnace 15, and the downstream side of the first exhaust duct 24 is gathered into a filter box 25. A second blower fan 26 that is connected and feeds exhaust gas in the direction of the filter box 25 is interposed in the collective portion. The filter box 25 purifies the exhaust discharged from the high temperature furnace 15.

更に、フィルタボックス25に循環路としての循環ダクト27の上流端が接続され、この循環ダクト27の中途が複数に分岐されて、各下流端が低温炉16の熱風導入口16aに接続されている。又、この循環ダクト27の集合部分にフィルタボックス25側からの熱風を熱風導入口16a方向へ送気する第3送風ファン28が介装されている。   Further, the upstream end of a circulation duct 27 as a circulation path is connected to the filter box 25, the middle of the circulation duct 27 is branched into a plurality of parts, and each downstream end is connected to the hot air inlet 16 a of the low temperature furnace 16. . In addition, a third blower fan 28 for sending hot air from the filter box 25 side toward the hot air introduction port 16a is interposed in the assembly portion of the circulation duct 27.

又、この低温炉16の排気口16bに第2排気路としての第2排気ダクト29の分岐された上流端がそれぞれ接続され、この第2排気ダクト29の下流側が集合されて加熱炉22に接続されている。更に、この第2排気ダクト29の集合部に、排気を加熱炉22側へ送気する第4送風ファン30が介装されている。   Further, the branched upstream end of a second exhaust duct 29 as a second exhaust path is connected to the exhaust port 16b of the low temperature furnace 16, and the downstream side of the second exhaust duct 29 is assembled and connected to the heating furnace 22. Has been. Further, a fourth blower fan 30 for sending exhaust gas to the heating furnace 22 side is interposed in the gathering portion of the second exhaust duct 29.

符号31は外気導入路としての外気導入ダクトであり、この外気導入ダクト31の下流側が第1分岐ダクト31aと第2分岐ダクト31bとに分岐され、第1分岐ダクト31aが加熱炉22に接続され、第2分岐ダクト31bがフィルタボックス25に接続されている。又、外気導入ダクト31に外気を各分岐ダクト31a,31b側へ送気する第5送風ファン32が介装されている。更に、この各分岐ダクト31a,31bに外気の流量を調整する外気流量調整手段としての第1、第2ダンパ33,34が各々介装されている。   Reference numeral 31 denotes an outside air introduction duct as an outside air introduction path. The downstream side of the outside air introduction duct 31 is branched into a first branch duct 31a and a second branch duct 31b, and the first branch duct 31a is connected to the heating furnace 22. The second branch duct 31b is connected to the filter box 25. In addition, a fifth blower fan 32 for supplying outside air to the branch ducts 31 a and 31 b is interposed in the outside air introduction duct 31. In addition, first and second dampers 33 and 34 as external air flow rate adjusting means for adjusting the flow rate of external air are interposed in the branch ducts 31a and 31b, respectively.

加熱炉22はバーナ35を備えており、このバーナ35にて通過する空気を加熱する。又、この加熱炉22内には通過する熱風を浄化するフィルタ36が内装されている。更に、図3、図4に示すように、第1送気ダクト21の第1送風ファン23上流側に、通過する熱風温度を検出する第1温度センサ37が接続されている。又、循環ダクト27の第3送風ファン28下流側に、通過する熱風の温度を検出する温度センサ38と、熱風の流量を計測する流量センサ39とが接続されている。尚、この両センサ38,39で、本発明の熱量計測手段が構成されている。   The heating furnace 22 includes a burner 35 and heats the air passing through the burner 35. In addition, a filter 36 for purifying hot air passing therethrough is built in the heating furnace 22. Further, as shown in FIGS. 3 and 4, a first temperature sensor 37 that detects the temperature of the passing hot air is connected to the upstream side of the first blower fan 23 of the first air supply duct 21. Further, a temperature sensor 38 that detects the temperature of hot air passing therethrough and a flow rate sensor 39 that measures the flow rate of hot air are connected to the circulation duct 27 downstream of the third blower fan 28. The two sensors 38 and 39 constitute the heat quantity measuring means of the present invention.

図5に示すように、上述した第1、第2ダンパ33,34の開度は、炉内温度制御手段としての炉内温度制御部41で制御される。この炉内温度制御部41は第1、第2温度センサ37,38で検出した熱風の温度と流量センサ39で計測した熱風の流量とに基づいて制御する。すなわち、第1温度センサ37で検出した加熱炉22による加熱後の熱風温度を読込み、この熱風温度が設定温度範囲に収まるように第1ダンパ33の開度を制御し、高温炉15の炉内温度を調整する。又、第2温度センサ38でフィルタボックス25から排出されて低温炉16に送気される熱風温度を検出すると共に、流量センサ39で熱風流量を計測し、その結果に基づいて、第2ダンパ34の開度を制御し、低温炉16に供給される熱風温度を調整して低温炉16の炉内温度を一定範囲に保持する。   As shown in FIG. 5, the opening degree of the first and second dampers 33 and 34 described above is controlled by a furnace temperature control unit 41 as furnace temperature control means. The in-furnace temperature control unit 41 performs control based on the hot air temperature detected by the first and second temperature sensors 37 and 38 and the hot air flow rate measured by the flow rate sensor 39. That is, the hot air temperature after heating by the heating furnace 22 detected by the first temperature sensor 37 is read, the opening degree of the first damper 33 is controlled so that the hot air temperature falls within the set temperature range, and the inside of the high temperature furnace 15 Adjust the temperature. Further, the temperature of the hot air discharged from the filter box 25 by the second temperature sensor 38 and sent to the low temperature furnace 16 is detected, and the flow rate of the hot air is measured by the flow rate sensor 39. Based on the result, the second damper 34 is measured. And the temperature of the hot air supplied to the low temperature furnace 16 is adjusted to keep the temperature inside the low temperature furnace 16 within a certain range.

上述した炉内温度制御部41にて制御される高温炉15、及び低温炉16の炉内温度は、具体的には、図6に示す高温炉内温度制御ルーチン、及び、図7に示す低温炉内温度制御ルーチンに従って調整される。この両ルーチンは並行に実行される。尚、各炉15,16には、塗布工程12で同一塗料が一括塗布された車体本体2とバンパ3,4とが、所定間隔毎に連続投入されており、各送風ファン23,26,28,30,32は連続運転されており、これにより各炉15,16に熱風が供給されている。   The in-furnace temperatures of the high temperature furnace 15 and the low temperature furnace 16 controlled by the in-furnace temperature control unit 41 are specifically the high temperature furnace temperature control routine shown in FIG. 6 and the low temperature shown in FIG. It is adjusted according to the furnace temperature control routine. Both routines are executed in parallel. The body 15 and the bumpers 3 and 4 to which the same paint is applied in the coating process 12 are continuously fed into the furnaces 15 and 16 at predetermined intervals. , 30 and 32 are operated continuously, whereby hot air is supplied to the furnaces 15 and 16.

先ず、高温炉内温度制御ルーチンについて説明する。このルーチンでは、ステップS1で第4送風ファン30の稼動により低温炉16を加温した排気を、第2排気ダクト29を経て加熱炉22に送給させる。又、ステップS2で第5送風ファン32の稼動により外気を、外気導入ダクト31を経て加熱炉22に導入する。尚、この外気導入ダクト33に介装されている第1ダンパ33の開度は、前回のルーチン実行時に調整されている。   First, the high temperature furnace temperature control routine will be described. In this routine, the exhaust gas heated in the low temperature furnace 16 by the operation of the fourth blower fan 30 in step S <b> 1 is supplied to the heating furnace 22 through the second exhaust duct 29. In step S 2, outside air is introduced into the heating furnace 22 through the outside air introduction duct 31 by the operation of the fifth blower fan 32. The opening degree of the first damper 33 interposed in the outside air introduction duct 33 is adjusted when the previous routine is executed.

そして、ステップS3へ進み、加熱炉22内にて低温炉16側からの排気と外気とを混合させ、その混合気をバーナ35の加熱により所定に昇温させる。尚、この加熱炉22にはフィルタ36が内装されており、このフィルタ36を通過する際に、混合気、特に、低温炉16からの排気に混入されている塗料等の粗ダストや揮発性有機化合物(VOC)等の不純物が除去されて浄化される。   Then, the process proceeds to step S <b> 3, the exhaust gas from the low temperature furnace 16 side and the outside air are mixed in the heating furnace 22, and the mixture is heated to a predetermined temperature by heating the burner 35. The heating furnace 22 is provided with a filter 36, and when passing through the filter 36, coarse dust such as paint mixed in an air-fuel mixture, particularly exhaust gas from the low-temperature furnace 16, or volatile organic matter. Impurities such as compound (VOC) are removed and purified.

そして、ステップS4へ進み、加熱炉22によって加熱された熱風を、第1送気ダクト21に介装されている第1送風ファン23の稼動により、第1送気ダクト21を経て高温炉15の下部に開口する複数の熱風導入口15aから炉内に送気し加熱する。   And it progresses to step S4, and the hot air heated by the heating furnace 22 passes through the 1st air supply duct 21 of the high temperature furnace 15 by the operation | movement of the 1st ventilation fan 23 interposed by the 1st air supply duct 21. Air is supplied into the furnace through a plurality of hot air inlets 15a that open to the lower portion and heated.

その間、ステップS5において、第1温度センサ37にて検出した第1送気ダクト21を通過する熱風の温度を読込み、ステップS6で、この熱風温度が予め設定した許容範囲に収まっているか、すなわち、高温炉15内を設定温度範囲に維持するだけの熱量を有しているか否かを調べる。   Meanwhile, in step S5, the temperature of the hot air passing through the first air supply duct 21 detected by the first temperature sensor 37 is read. In step S6, whether the hot air temperature is within a preset allowable range, that is, It is checked whether or not it has a quantity of heat sufficient to maintain the inside of the high temperature furnace 15 in the set temperature range.

そして、熱風温度が許容範囲に収まっている場合、ステップS8へ進む。又、熱風温度が許容範囲から外れている場合はステップS7へ分岐し、例えば許容範囲の中心値を目標熱風温度として設定し、この目標熱風温度と第1温度センサ37で検出した熱風温度との差分に基づき、第1ダンパ33の開度を制御し、熱風温度が許容範囲に収まるように調整する。すなわち、第1温度センサ37で検出した熱風温度が許容範囲を下回っている場合、第1ダンパ33の開度を絞り、バーナ35で加熱する混合気の低温炉16側からの排気に対する外気の比率を低くする。その結果、外気による混合気の温度低下が抑制され、その分、熱風の温度を上昇させて、熱風温度が許容範囲に収まるようにフィードバック制御を行う。一方、熱風温度が許容範囲を上回っている場合、第1ダンパ33の開度を大きくして、加熱炉22に供給する外気流量を増加させて混合気の温度を積極的に低下させて、熱風温度が許容範囲に収まるようにフィードバック制御を行う。   If the hot air temperature is within the allowable range, the process proceeds to step S8. If the hot air temperature is out of the allowable range, the process branches to step S7. For example, the center value of the allowable range is set as the target hot air temperature, and the target hot air temperature and the hot air temperature detected by the first temperature sensor 37 are set. Based on the difference, the opening degree of the first damper 33 is controlled and adjusted so that the hot air temperature falls within the allowable range. That is, when the hot air temperature detected by the first temperature sensor 37 is below the allowable range, the opening ratio of the first damper 33 is reduced, and the ratio of the outside air to the exhaust from the low temperature furnace 16 side of the mixture heated by the burner 35 Lower. As a result, the temperature drop of the air-fuel mixture due to the outside air is suppressed, and the temperature of the hot air is increased accordingly, and feedback control is performed so that the hot air temperature falls within the allowable range. On the other hand, when the hot air temperature exceeds the allowable range, the opening degree of the first damper 33 is increased, the flow rate of the outside air supplied to the heating furnace 22 is increased, and the temperature of the air-fuel mixture is actively reduced, so that the hot air Feedback control is performed so that the temperature falls within the allowable range.

その結果、高温炉15内の温度(炉内温度)は複数の熱風導入口15aから吹き出される熱風により所定の高温に維持される。   As a result, the temperature in the high temperature furnace 15 (furnace temperature) is maintained at a predetermined high temperature by the hot air blown from the plurality of hot air inlets 15a.

そして、ステップS8へ進み、高温炉15内を加熱した排気を排気口15bから第1排気ダクト24に介装されている第2送風ファン26の稼動によりフィルタボックス25へ送気して、ルーチンを抜ける。フィルタボックス25は、高温炉15からの排気に混入されている塗料等の粗ダストや揮発性有機化合物(VOC)等の不純物を除去して浄化すると共に、排気と外気とを混合させる。従って、このフィルタボックス25は、本発明の混合ボックスとしての機能を備えている。   Then, the process proceeds to step S8, and the exhaust gas heated in the high temperature furnace 15 is supplied to the filter box 25 by the operation of the second blower fan 26 interposed in the first exhaust duct 24 from the exhaust port 15b. Exit. The filter box 25 removes and purifies impurities such as coarse dust such as paint and volatile organic compounds (VOC) mixed in the exhaust from the high temperature furnace 15 and mixes the exhaust and the outside air. Therefore, the filter box 25 has a function as a mixing box of the present invention.

次に、低温炉内温度制御ルーチンについて説明する。このルーチンでは、先ず、ステップS11で第3送風ファン28の稼動により、フィルタボックス25に供給された高温炉15からの排気熱と外気導入ダクト31を経て導入された外気とが混合されて生成された熱風を、低温炉16の底部に開口されている複数の熱風導入口16aに循環ダクト27を経て送気する。そして、この複数の熱風導入口16aから吹き出された熱風により炉内を加熱する。   Next, the low temperature furnace temperature control routine will be described. In this routine, first, the exhaust air from the high temperature furnace 15 supplied to the filter box 25 and the outside air introduced through the outside air introduction duct 31 are mixed and generated by the operation of the third blower fan 28 in step S11. The heated hot air is sent to the plurality of hot air inlets 16 a opened at the bottom of the low temperature furnace 16 through the circulation duct 27. Then, the inside of the furnace is heated by the hot air blown out from the plurality of hot air inlets 16a.

その間、ステップS12では循環ダクト27を通過する熱風温度を第2温度センサ38で検出し、又、ステップS13では通過する熱風の単位時間当たりの流量を流量センサ39で計測する。そして、ステップS14へ進み、予め設定されている低温炉16の目標炉温と循環ダクト27を通過する熱風の温度との差温、及び循環ダクト27を通過する単位時間当たりの流量に基づき低温炉16に供給する熱量を算出し、この熱量が所定範囲に収まっているか否かを調べる。換言すれば、供給する熱量が低温炉16を目標炉温に対して所定の温度範囲に維持させることができるものであるか否かを調べる。   Meanwhile, in step S12, the temperature of the hot air passing through the circulation duct 27 is detected by the second temperature sensor 38, and in step S13, the flow rate per unit time of the hot air passing is measured by the flow rate sensor 39. Then, the process proceeds to step S14, and the low temperature furnace is set based on the preset temperature difference between the target furnace temperature of the low temperature furnace 16 and the temperature of the hot air passing through the circulation duct 27 and the flow rate per unit time passing through the circulation duct 27. The amount of heat supplied to 16 is calculated, and it is checked whether this amount of heat is within a predetermined range. In other words, it is examined whether or not the amount of heat supplied can maintain the low temperature furnace 16 in a predetermined temperature range with respect to the target furnace temperature.

そして、この熱量が許容範囲に収まっている場合は、そのままステップS16へ進む。又、許容範囲から外れている場合は、ステップS15へ分岐し、熱量を外気により低下させるための目標流量を算出し、第2ダンパ34の開度を制御して、低温炉16に供給する外気流量が目標流量となるように調整する。   And when this calorie | heat amount is settled in the tolerance | permissible_range, it progresses to step S16 as it is. If it is outside the allowable range, the process branches to step S15, the target flow rate for reducing the amount of heat by the outside air is calculated, the opening degree of the second damper 34 is controlled, and the outside air supplied to the low temperature furnace 16 is calculated. Adjust the flow rate to the target flow rate.

高温炉15内を加熱した後の排気の温度及び流量が安定している場合、第1ダンパ33の開度はほぼ一定状態を維持している。従って、フィルタボックス25に流入する排気温度及び流量もほぼ一定している。   When the temperature and flow rate of the exhaust gas after heating the inside of the high-temperature furnace 15 is stable, the opening degree of the first damper 33 is maintained in a substantially constant state. Accordingly, the exhaust temperature and flow rate flowing into the filter box 25 are also substantially constant.

その結果、第2温度センサ38で検出する熱風温度、及び流量センサ39で検出する熱風流量は、第2ダンパ34の開度に依存し、第2ダンパ34の開度を大きくすれば流量は増加し、熱風温度は低下する。一方、第2ダンパ34の開度を絞れば流量は減少し、熱風温度は上昇する。例えば、高温炉15を加熱する熱風の温度が170°で、低温炉16を加熱する熱風の温度が120°に設定されている場合、当然、高温炉15から排出される排気熱の温度は低温炉16の炉内温度よりも高い。そのため、第2ダンパ34の開度を制御することで低温炉16に供給するために必要とする熱風の熱量を得ることができる。   As a result, the hot air temperature detected by the second temperature sensor 38 and the hot air flow rate detected by the flow sensor 39 depend on the opening degree of the second damper 34, and the flow rate increases if the opening degree of the second damper 34 is increased. However, the hot air temperature decreases. On the other hand, if the opening degree of the second damper 34 is reduced, the flow rate decreases and the hot air temperature rises. For example, when the temperature of the hot air for heating the high temperature furnace 15 is 170 ° and the temperature of the hot air for heating the low temperature furnace 16 is set to 120 °, the temperature of the exhaust heat exhausted from the high temperature furnace 15 is naturally low. The temperature inside the furnace of the furnace 16 is higher. Therefore, by controlling the opening degree of the second damper 34, it is possible to obtain the amount of hot air necessary for supplying the low temperature furnace 16.

上述したステップS15では、ステップS14で求めた熱量と低温炉16の目標炉温とに基づき、演算或いはマップ検索によって、低温炉16に供給する熱量が許容範囲に収まるように第2ダンパ34の開度を調整する。その後、ステップS14或いはステップS15からステップS16へ進むと、低温炉16内を加熱した後の排気を加熱炉22に送気し、還流させてルーチンを抜ける。   In step S15 described above, the second damper 34 is opened so that the amount of heat supplied to the low temperature furnace 16 is within an allowable range by calculation or map search based on the heat amount obtained in step S14 and the target furnace temperature of the low temperature furnace 16. Adjust the degree. Thereafter, when the process proceeds from step S14 or step S15 to step S16, the exhaust gas after the inside of the low temperature furnace 16 is heated is sent to the heating furnace 22 to be refluxed and the routine is exited.

このように、本実施形態では、高温炉15からの排気熱を低温炉16に供給して加熱するに際し、この排気熱を外気と混合させることで冷却して、低温炉16を加熱する最適な熱風温度に調整するようにしたので、低温炉16の炉内温度を容易に調整することができる。その結果、低温炉16の炉内温度の管理が容易となり、塗装完了後のバンパ3,4の色相を一定の範囲に収めることが可能となり、色相照合部17で照合される車体本体2とバンパ3,4との色差を許容範囲に収めることができる。従って、色相調整に要する負担を大幅に軽減することができ、生産効率の向上を図ることができる。   As described above, in this embodiment, when the exhaust heat from the high temperature furnace 15 is supplied to the low temperature furnace 16 and heated, the exhaust heat is cooled by mixing with the outside air, and the low temperature furnace 16 is optimally heated. Since the temperature is adjusted to the hot air temperature, the temperature inside the low temperature furnace 16 can be easily adjusted. As a result, the temperature inside the low-temperature furnace 16 can be easily managed, and the hues of the bumpers 3 and 4 after the completion of painting can be kept within a certain range. The color difference between 3 and 4 can be within an allowable range. Therefore, the burden required for hue adjustment can be greatly reduced, and the production efficiency can be improved.

[第2実施形態]
図8、図9に本発明の第2実施形態を示す。本実施形態では、高温炉15と低温炉16とを隣接させた状態で配設して両炉15,16を一体化し、この両炉15,16に熱源供給系統を形成すると共に、高温炉15に対しては熱風を上部から吹き出させるようにしたものである。尚、第1実施形態と同一の構成部分については同一の符号を付して説明を省略、或いは簡略化する。
[Second Embodiment]
8 and 9 show a second embodiment of the present invention. In the present embodiment, the high-temperature furnace 15 and the low-temperature furnace 16 are arranged adjacent to each other, and both the furnaces 15 and 16 are integrated, a heat source supply system is formed in both the furnaces 15 and 16, and the high-temperature furnace 15 In contrast, hot air is blown out from above. Note that the same components as those of the first embodiment are denoted by the same reference numerals, and description thereof is omitted or simplified.

図8に示すように、高温炉15と低温炉16とが流路空間を空けて隣接されている。又、図9に示すように、高温炉15の上部に第1調整部15cが設けられ、下部に第2調整部15dが設けられている。更に、低温炉16の下部に第3調整部16cが設けられている。   As shown in FIG. 8, the high-temperature furnace 15 and the low-temperature furnace 16 are adjacent to each other with a passage space therebetween. Moreover, as shown in FIG. 9, the 1st adjustment part 15c is provided in the upper part of the high temperature furnace 15, and the 2nd adjustment part 15d is provided in the lower part. Further, a third adjustment unit 16 c is provided at the lower part of the low temperature furnace 16.

又、両炉15,16間に形成した流路空間の下部を第1排気ダクト24とし、フィルタボックス25を介した上方を循環ダクト27としている。更に、低温炉16の外壁から、循環ダクト27の上方であって高温炉15と低温炉16の間に形成した流路空間を第2排気ダクト29としている。又、第1調整部15cに第1送気ダクト21の下流端が接続され、一方、第2排気ダクト29の下流端が加熱炉22に連通されている。   The lower part of the flow path space formed between the furnaces 15 and 16 is a first exhaust duct 24, and the upper part through the filter box 25 is a circulation duct 27. Furthermore, a flow path space formed between the high temperature furnace 15 and the low temperature furnace 16 above the circulation duct 27 from the outer wall of the low temperature furnace 16 is used as a second exhaust duct 29. The downstream end of the first air supply duct 21 is connected to the first adjustment unit 15 c, while the downstream end of the second exhaust duct 29 is communicated with the heating furnace 22.

第1、第2調整部15c,15dは調整機能を有しており、高温炉15に流入、或いは高温炉15から流出する熱風(内気)の湿度、VOC濃度、ダストクリーン度等を更に調整する。又、第3調整部16cは低温炉16を加熱した後の熱風に混入されている異物を除去する物理フィルタや調整機能を有しており、調整機能としては、蒸気圧線図から低温時の飽和密度が高温時の飽和密度よりも高いことを利用して水蒸気及びVOCを回収する。   The first and second adjustment units 15c and 15d have an adjustment function, and further adjust the humidity, VOC concentration, dust cleanliness, etc. of hot air flowing into or out of the high temperature furnace 15 (inside air). . The third adjusting unit 16c has a physical filter and an adjusting function for removing foreign matters mixed in the hot air after heating the low temperature furnace 16, and the adjusting function is as follows. Steam and VOC are recovered utilizing the fact that the saturation density is higher than the saturation density at high temperature.

尚、図示しないが、第1送気ダクト21に第1温度センサ37が接続され、循環ダクト27に第2温度センサ38、流量センサ39が接続されている。又、各ダクト21,24,27,29,31に第1〜第5送風ファン23,26,28,30,32が介装されている。更に、高温炉15及び低温炉16の炉内温度制御は、上述した第1実施形態と同じであるため説明を省略する。   Although not shown, a first temperature sensor 37 is connected to the first air supply duct 21, and a second temperature sensor 38 and a flow rate sensor 39 are connected to the circulation duct 27. In addition, the first to fifth blower fans 23, 26, 28, 30 and 32 are interposed in the ducts 21, 24, 27, 29 and 31. Furthermore, the temperature control inside the high temperature furnace 15 and the low temperature furnace 16 is the same as that in the first embodiment described above, and thus the description thereof is omitted.

このような構成では、第1ダンパ33の開度によって流量が調整された外気と第2排気ダクト29を経て流入した、低温炉16を加熱した後の排気が、加熱炉22を通過する際に混合されて所定に加熱された熱風となり、第1送気ダクト21を経て第1調整部15cに吹き出される。   In such a configuration, when the outside air whose flow rate is adjusted by the opening degree of the first damper 33 and the exhaust gas after flowing through the second exhaust duct 29 after heating the low temperature furnace 16 passes through the heating furnace 22. The hot air is mixed and heated to a predetermined temperature, and blown out through the first air supply duct 21 to the first adjusting portion 15c.

第1調整部15cでは、流入した熱風(内気)の湿度、VOC濃度、ダストクリーン度等を調整して、高温炉15へ吹き出させ、高温炉15を所定に加熱する。そして、加熱した後の排気を第2調整部15dへ送り、その湿度、VOC濃度、ダストクリーン度等を調整した後、第1排気ダクト24に送られ、第2ダンパ34の開度によって流量が調整された外気と共にフィルタボックス25に送気される。   In the 1st adjustment part 15c, the humidity of the inflowing hot air (inside air), VOC density | concentration, a dust clean degree, etc. are adjusted, it blows off to the high temperature furnace 15, and the high temperature furnace 15 is heated predetermined. Then, the heated exhaust is sent to the second adjusting unit 15d, and after adjusting the humidity, VOC concentration, dust cleanness, etc., the exhaust is sent to the first exhaust duct 24, and the flow rate is controlled by the opening of the second damper 34. It is sent to the filter box 25 together with the adjusted outside air.

フィルタボックス25に送られた排気と外気との混合気は、所定に混合されると共に、不純物を除去して浄化した後、循環ダクト27を経て隣接する低温炉16に吹き出されて、炉内を加熱する。又、この低温炉16は、ダクト空間を介して高温炉15に隣接されているため、第1排気ダクト24と循環ダクト27とを通過する熱風の輻射熱によっても加熱される。   The air-fuel mixture of the exhaust gas and the outside air sent to the filter box 25 is mixed in a predetermined manner and purified by removing impurities, and then blown out to the adjacent low-temperature furnace 16 through the circulation duct 27 to pass through the inside of the furnace. Heat. Further, since the low temperature furnace 16 is adjacent to the high temperature furnace 15 through the duct space, the low temperature furnace 16 is also heated by radiant heat of hot air passing through the first exhaust duct 24 and the circulation duct 27.

そして、低温炉16内を所定に加熱した熱風は第3調整部16cにて異物が除去されると共に、水蒸気及びVOCが回収されて、第2排気ダクト29から加熱炉22に還流される。   The hot air heated to a predetermined temperature in the low-temperature furnace 16 removes foreign matter by the third adjusting unit 16c, collects water vapor and VOC, and returns to the heating furnace 22 from the second exhaust duct 29.

このように、本実施形態では、高温炉15と低温炉16とをダクト空間を介して隣接させ、このダクト空間に第1排気ダクト24と循環ダクト27とを形成したので、このダクト24,27を通過する熱風の輻射熱によっても低温炉16内を加熱させることができ、低温炉16内の加熱効率が向上する。又、第2排気ダクト29を低温炉16と高温炉15との外壁に形成したので、設備全体のコンパクト化を実現することができる。   As described above, in this embodiment, the high temperature furnace 15 and the low temperature furnace 16 are adjacent to each other through the duct space, and the first exhaust duct 24 and the circulation duct 27 are formed in the duct space. The inside of the low-temperature furnace 16 can be heated also by the radiant heat of the hot air passing through the heating chamber, and the heating efficiency in the low-temperature furnace 16 is improved. In addition, since the second exhaust duct 29 is formed on the outer wall of the low temperature furnace 16 and the high temperature furnace 15, the entire equipment can be made compact.

[第3実施形態]
図10に本発明の第3実施形態を示す。本実施形態は上述した第2実施形態の変形例である。尚、第2実施形態と同一の構成部分については同一の符号を付して説明を省略する。
[Third Embodiment]
FIG. 10 shows a third embodiment of the present invention. This embodiment is a modification of the second embodiment described above. In addition, about the component same as 2nd Embodiment, the same code | symbol is attached | subjected and description is abbreviate | omitted.

本実施形態では、加熱炉22に接続する第1送気ダクト21の下流端、及び低温炉16に接続する第2排気ダクト29の上流端を、高温炉15と低温炉16との平面視において一方(図においてはラインの流れに対して上流側)に偏倚した位置に開口させている。   In the present embodiment, the downstream end of the first air supply duct 21 connected to the heating furnace 22 and the upstream end of the second exhaust duct 29 connected to the low temperature furnace 16 are viewed in a plan view of the high temperature furnace 15 and the low temperature furnace 16. It is opened at a position biased on the one side (upstream side with respect to the line flow in the figure).

又、互いに隣接する高温炉15と低温炉16間に形成したダクト空間に設けた第1排気ダクト24の上流側と循環ダクト27の下流側とを、平面視において他方(図においてはラインの下流側)へ偏倚した位置で、高温炉15と低温炉16とに接続させたものである。   Further, the upstream side of the first exhaust duct 24 and the downstream side of the circulation duct 27 provided in the duct space formed between the high-temperature furnace 15 and the low-temperature furnace 16 adjacent to each other are shown in plan view in the other (downstream of the line in the figure). The high temperature furnace 15 and the low temperature furnace 16 are connected at a position biased to the side).

これにより、第1送気ダクト21から高温炉15に吹き出された熱風は、高温炉15内を上部から下部方向へ斜めに流れるため、炉内を効率良く加熱することができる。同様に、循環ダクト27から低温炉16に吹き出された熱風は、炉内を下部から上部方向へ斜めに流れるため、この場合も炉内を効率良く加熱することができる
尚、本発明は、上述した実施形態に限るものではなく、例えば、加熱炉22にベントを設け、外気導入ダクト31から各ダンパ33,34を介して導入される外気分の圧力上昇を調整するようにしても良い。
Thereby, the hot air blown out from the first air supply duct 21 to the high temperature furnace 15 flows obliquely in the high temperature furnace 15 from the upper part to the lower part, so that the inside of the furnace can be efficiently heated. Similarly, since the hot air blown out from the circulation duct 27 to the low temperature furnace 16 flows obliquely from the lower part to the upper part in the furnace, the inside of the furnace can be efficiently heated in this case as well. For example, the heating furnace 22 may be provided with a vent to adjust the pressure increase of the outside air introduced from the outside air introduction duct 31 via the dampers 33 and 34.

1…塗装設備、
2…車体本体、
3…フロントバンパ、
4…リヤバンパ、
12…塗布工程、
13…分離乾燥焼付工程、
14…車体分離部、
15…高温乾燥焼付炉、
15a,16a…熱風導入口、
15b,16b…排気口、
15c…第1調整部、
15d…第2調整部、
16…低温乾燥焼付炉、
16c…第3調整部
17…色相照合部、
18…色相調整部、
19…車体集成部、
21…第1送気ダクト、
22…加熱炉、
23…第1送風ファン、
24…第1排気ダクト、
25…フィルタボックス、
26…第2送風ファン、
27…循環ダクト、
28…第3送風ファン、
29…第2排気ダクト、
30…第4送風ファン、
31…外気導入ダクト、
31a…第1分岐ダクト、
31b…第2分岐ダクト、
32…第5送風ファン、
33…第1ダンパ、
34…第2ダンパ、
35…バーナ、
36…フィルタ、
37…第1温度センサ、
38…第2温度センサ、
39…流量センサ、
41…炉内温度制御部、
Jt1,Jt2…搬送治具、
M1…車体
1 ... painting equipment,
2 ... Body body,
3 ... Front bumper,
4 ... Rear bumper,
12 ... coating process,
13: Separation drying baking process,
14 ... body separation part,
15 ... high temperature drying baking furnace,
15a, 16a ... hot air inlet,
15b, 16b ... exhaust port,
15c ... 1st adjustment part,
15d ... 2nd adjustment part,
16 ... Low-temperature drying baking furnace,
16c ... 3rd adjustment part 17 ... Hue collation part,
18 ... Hue adjustment section,
19 ... Body assembly part,
21 ... First air duct,
22 ... heating furnace,
23. First blower fan,
24. First exhaust duct,
25 ... Filter box,
26 ... the second blower fan,
27 ... circulation duct,
28. Third fan,
29 ... second exhaust duct,
30 ... Fourth fan,
31 ... outside air introduction duct,
31a ... 1st branch duct,
31b ... the second branch duct,
32 ... Fifth fan
33 ... first damper,
34 ... The second damper,
35 ... Burner,
36 ... filter,
37 ... first temperature sensor,
38 ... second temperature sensor,
39 ... Flow sensor,
41 ... Furnace temperature controller,
Jt1, Jt2 ... Conveying jig,
M1 ... Body

Claims (4)

塗料を塗布した後の金属製部品を乾燥焼付けする高温炉と、
塗料を塗布した後の樹脂製部品を乾燥焼付けする低温炉と、
前記高温炉に熱風を供給する加熱炉と、
前記高温炉を加熱した前記熱風を排出する第1排気路と、
前記第1排気路からの排気を前記低温炉に供給する循環路と、
前記低温炉からの排気を前記加熱炉へ循環させる第2排気路と
を有する塗装乾燥設備において、
前記第1排気路と前記循環路とが接続される混合ボックスと、
前記混合ボックスに接続された外気導入路と、
前記外気導入路に介装されて前記混合ボックスに導入する外気流量を調整する外気流量調整手段と、
前記循環路を通過する熱風の熱量を計測する熱量計測手段と、
前記熱量計測手段で計測した熱量と予め設定されている前記低温炉内の目標炉温とに基づき前記外気流量調整手段の流量を制御して前記循環路を通過する熱風の熱量を調整する炉内温度制御手段と
を更に備えることを特徴とする塗装乾燥設備。
A high-temperature furnace for drying and baking metal parts after applying paint,
A low-temperature furnace for drying and baking resin parts after applying paint;
A heating furnace for supplying hot air to the high temperature furnace;
A first exhaust path for discharging the hot air that heated the high-temperature furnace;
A circulation path for supplying exhaust from the first exhaust path to the low temperature furnace;
In the paint drying facility having a second exhaust passage for circulating the exhaust from the low temperature furnace to the heating furnace,
A mixing box to which the first exhaust path and the circulation path are connected;
An outside air introduction path connected to the mixing box;
An outside air flow rate adjusting means that adjusts an outside air flow rate that is interposed in the outside air introduction path and is introduced into the mixing box;
A calorific value measuring means for measuring the calorific value of the hot air passing through the circulation path;
In the furnace, the flow rate of the outside air flow rate adjusting means is controlled based on the heat quantity measured by the heat quantity measuring means and the preset target furnace temperature in the low temperature furnace to adjust the heat quantity of the hot air passing through the circulation path A paint drying facility, further comprising a temperature control means.
前記高温炉と前記低温炉とが流路空間を介して隣接され、
前記流路空間に前記第1排気路と前記循環路とが形成されていると共に、前記第1排気路と前記循環路との間に前記混合ボックスが介装されている
ことを特徴とする請求項1記載の塗装乾燥設備。
The high temperature furnace and the low temperature furnace are adjacent to each other through a flow path space,
The first exhaust path and the circulation path are formed in the flow path space, and the mixing box is interposed between the first exhaust path and the circulation path. Item 1. A paint drying facility according to item 1.
前記第1排気路が前記流路空間の下部に形成されていると共に上流が前記高温炉の下部に接続され、
前記循環路が前記流路空間の上部に形成されていると共に下流が前記低温炉の上部に接続され、
前記流路空間の前記第1排気路と前記循環路との間に前記混合ボックスが介装され、
前記高温炉の上部に前記加熱炉からの熱風を前記高温炉に吹き出させる第1送気路が接続され、
前記低温炉の下部に前記第2排気路の上流が接続されている
ことを特徴とする請求項2記載の塗装乾燥設備。
The first exhaust path is formed in the lower part of the flow path space and the upstream is connected to the lower part of the high temperature furnace,
The circulation path is formed in the upper part of the flow path space and the downstream is connected to the upper part of the low temperature furnace,
The mixing box is interposed between the first exhaust path and the circulation path in the flow path space,
A first air supply path for blowing hot air from the heating furnace to the high temperature furnace is connected to an upper portion of the high temperature furnace,
The paint drying facility according to claim 2, wherein an upstream side of the second exhaust passage is connected to a lower portion of the low-temperature furnace.
前記第1送気路の下流端と前記第1排気路の上流端とが、前記高温炉に対してラインの流れ方向において異なる位置で接続され、
前記循環路の下流端と前記第2排気路の上流端とが、前記低温炉に対してラインの流れ方向において異なる位置で接続されている
ことを特徴とする請求項2或いは3に記載の塗装乾燥設備。
The downstream end of the first air supply path and the upstream end of the first exhaust path are connected to the high temperature furnace at different positions in the line flow direction,
The coating according to claim 2 or 3, wherein a downstream end of the circulation path and an upstream end of the second exhaust path are connected to the low temperature furnace at different positions in a line flow direction. Drying equipment.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2024524890A (en) * 2022-05-19 2024-07-09 エルジー エナジー ソリューション リミテッド Method and system for drying battery components

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2024524890A (en) * 2022-05-19 2024-07-09 エルジー エナジー ソリューション リミテッド Method and system for drying battery components
JP7754954B2 (en) 2022-05-19 2025-10-15 エルジー エナジー ソリューション リミテッド Method and system for drying battery components

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