JP5386008B2 - Dehumidification and organic solvent treatment system for painting room - Google Patents

Dehumidification and organic solvent treatment system for painting room Download PDF

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JP5386008B2
JP5386008B2 JP2012118755A JP2012118755A JP5386008B2 JP 5386008 B2 JP5386008 B2 JP 5386008B2 JP 2012118755 A JP2012118755 A JP 2012118755A JP 2012118755 A JP2012118755 A JP 2012118755A JP 5386008 B2 JP5386008 B2 JP 5386008B2
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organic solvent
painting
coating
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air
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JP2012179602A (en
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憲秀 門井
利暁 藤井
幸人 檜垣
和幸 檜垣
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IMABARI SHIPBUILDING CO., LTD.
JFE Denki Corp
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JFE Mechanical Co Ltd
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Description

本発明は、船体ブロック、橋梁ブロックを塗装するための塗装室に外気を除湿して供給すると共に、塗装室で発生する有機溶剤を処理して大気中に排気する塗装室用除湿及び有機溶剤処理システムに関する。   The present invention relates to a dehumidification and organic solvent treatment for a painting chamber in which the outside air is dehumidified and supplied to a painting chamber for painting a hull block and a bridge block, and the organic solvent generated in the painting chamber is treated and exhausted to the atmosphere. About the system.

造船所、橋梁物工場では、船や橋梁を輪切りにしたような船体ブロック、橋梁ブロックにエアーブラスト及び塗装を行う(例えば特許文献1参照)。船体ブロック、橋梁ブロックは約20m×20m×10mH程度の大きさなので、ブラスト室、塗装室はそれ以上の例えば50m×35m×17mHの大きさをもつ。船体ブロック、橋梁ブロックは台車に載せられて塗装室に搬入される。塗装に先立ってブラスト室では、船体ブロック、橋梁ブロックにエアーブラストを行う。塗装室では、人力で塗装用のスプレーガンを用いて塗装が行われる。   In shipyards and bridge factories, air blasting and painting are performed on hull blocks and bridge blocks that are formed by cutting a ship or a bridge (see, for example, Patent Document 1). Since the hull block and the bridge block are approximately 20 m × 20 m × 10 mH in size, the blast chamber and the painting chamber have a size of, for example, 50 m × 35 m × 17 mH beyond that. The hull block and bridge block are placed on a carriage and carried into the painting room. Prior to painting, air blasting is performed on the hull block and bridge block in the blast room. In the painting room, painting is performed manually using a spray gun for painting.

船体ブロック、橋梁ブロックは事前にエアーブラストがなされているので、塗装する際に船体ブロック、橋梁ブロックは生の金属が露出している状態になっている。造船業界の塗装指針には、船体ブロック、橋梁ブロックが錆びるのを防止するため、塗装室の雰囲気湿度を所定以下、例えば85%以下にし、且つ冬場の雰囲気温度を所定温度以上、例えば5℃以上にすることが定められている。上述の温度・湿度の条件を満たそうとすると、除湿機で塗装室の温度・湿度を管理する必要がある。   Since the hull block and bridge block are air-blasted in advance, the hull block and bridge block are exposed to raw metal when they are painted. According to the coating guidelines in the shipbuilding industry, to prevent the hull block and bridge block from rusting, the atmospheric humidity in the painting room should be lower than a predetermined value, for example, 85% or lower, and the atmospheric temperature in winter should be higher than a predetermined temperature, for example, 5 ° C or higher. It is stipulated to be. In order to satisfy the above-described temperature / humidity conditions, it is necessary to manage the temperature / humidity of the coating room with a dehumidifier.

そのうえ、塗装室内で塗料(ペンキ)を塗ると、塗料中の有機溶剤(シンナ)が塗装室内で発生する。塗装を行う人の環境を守るため、労働基準局は塗装室内での有機溶剤の濃度を所定以下に下げることを定めている。そして、大気に排気される有機溶剤の量を低減するため、大気汚染防止法は大気中へ排出される有機溶剤の濃度を所定以下に下げることを定めている。それゆえ、塗装室内で発生した有機溶剤を含む空気を有機溶剤除去装置で除去して大気中に排出する必要がある。   In addition, when paint (paint) is applied in the paint chamber, an organic solvent (thinner) in the paint is generated in the paint chamber. In order to protect the environment of painters, the Labor Standards Bureau stipulates that the concentration of organic solvents in the paint chamber be reduced below a predetermined level. In order to reduce the amount of the organic solvent exhausted to the atmosphere, the Air Pollution Control Law stipulates that the concentration of the organic solvent exhausted to the atmosphere be lowered to a predetermined level or less. Therefore, it is necessary to remove the air containing the organic solvent generated in the coating chamber with an organic solvent removing device and discharge it to the atmosphere.

上記に記載の温度・湿度の条件も満たし、且つ有機溶剤の濃度も低減するため、図5に示されるように、従来の塗装室の換気システムには、外気を除湿して塗装室1に供給する除湿機2と、塗装室1で発生する有機溶剤を含む空気を処理して大気中に排気する有機溶剤除去装置3と、が組み込まれていた。   In order to satisfy the temperature and humidity conditions described above and reduce the concentration of organic solvent, the conventional painting room ventilation system dehumidifies the outside air and supplies it to the painting room 1 as shown in FIG. The dehumidifier 2 that performs this process and the organic solvent removal device 3 that processes the air containing the organic solvent generated in the coating chamber 1 and exhausts it into the atmosphere have been incorporated.

特公昭58−47231号公報Japanese Patent Publication No.58-47231

しかし、除湿機及び有機溶剤除去装置の風量は、室内の体積×換気回数(室内の空気を1時間当たり交換できる回数)によって定められるので、室内の体積及び換気回数のいずれも大きい塗装室用換気システムでは、除湿機及び有機溶剤除去装置共にの風量が必然的に大きくなり、除湿機及び有機溶剤除去装置が大型化する。除湿機及び有機溶剤除去装置の大型化は、初期費用の増大のみならずランニングコストの増大を招く。例えば塗装室の大きさが50m×35m×17mHであるとし、換気回数を5回/hにとると、除湿機及び有機溶剤除去装置の風量は共に、50×35×17×5/60=2480m/minになってしまう。 However, the air volume of the dehumidifier and the organic solvent removal device is determined by the volume of the room x the number of ventilations (the number of times the room air can be exchanged per hour). In the system, the air volume of both the dehumidifier and the organic solvent removal device inevitably increases, and the dehumidifier and the organic solvent removal device become larger. Increasing the size of the dehumidifier and the organic solvent removing apparatus not only increases the initial cost but also increases the running cost. For example, if the size of the painting room is 50 m x 35 m x 17 mH, and the ventilation frequency is 5 times / h, the air volume of the dehumidifier and the organic solvent removal device is 50 x 35 x 17 x 5/60 = 2480 m. 3 / min.

ところで、一概に塗装室といっても塗装作業の工程上、塗装工程の後に必ず乾燥工程が行われる。このため塗装室は、塗装を行っている部屋と乾燥を行っている部屋とに分かれる。塗装作業員が居るのは塗装を行っている部屋だけで、乾燥を行っている部屋は無人になる。そして、塗装作業全体を効率的に行うため、複数の塗装室が一組にされ、作業員によって塗装が行われるのはそのうちの一部屋のみで残りの部屋では乾燥が行われる。例えばA,Bの二つの塗装室が一組にされる場合、塗装作業員が塗装作業を行うのはA又はBの塗装室のみであり、残りの塗装室では乾燥工程が行われる。また、A,B,Cの三つの塗装室が一組にされる場合、塗装作業員が塗装作業を行うのはA,B,Cのうちの一つの塗装室のみであり、残りの二つの塗装室では乾燥工程が行われる。   By the way, even if it is generally called a painting chamber, a drying process is always performed after the painting process because of the painting work process. For this reason, the painting room is divided into a room for painting and a room for drying. The painting workers are only in the rooms where painting is performed, and the rooms where drying is performed are unattended. In order to efficiently perform the entire painting operation, a plurality of coating chambers are combined into one set, and only one of the chambers is coated by an operator, and drying is performed in the remaining chambers. For example, when two painting chambers A and B are combined, the painting worker performs painting work only in the painting chamber A or B, and the drying process is performed in the remaining painting chambers. When the three painting chambers A, B, and C are combined into one set, the painting worker performs painting work only in one of the painting chambers A, B, and C, and the remaining two A drying process is performed in the painting room.

塗装が行われている塗装室では、有機溶剤の発生量も大きく、且つ作業員もいるので、有機溶剤除去装置の処理能力を上げる必要がある。他方、乾燥が行われている塗装室では、有機溶剤の発生量も少ないし、且つ作業員もいないので、有機溶剤除去装置の処理能力をそれほど上げる必要もない。従来の有機溶剤除去装置はこのような塗装室の使用状況に着目したものといえず、有機溶剤除去装置が大型化し易く、初期費用及びランニングコストの増大を招いていた。   In a painting room where painting is performed, the amount of organic solvent generated is large, and there are workers, so it is necessary to increase the processing capacity of the organic solvent removing apparatus. On the other hand, in the coating room where drying is performed, the amount of organic solvent generated is small and there are no workers, so that it is not necessary to increase the processing capacity of the organic solvent removing device so much. The conventional organic solvent removal apparatus cannot be said to have been focused on the use situation of such a coating chamber, and the organic solvent removal apparatus is likely to be large-sized, leading to an increase in initial cost and running cost.

そこで、本発明の目的は、塗装室の使用状況に着目し、有機溶剤除去装置が大型化することのない塗装室用有機溶剤処理システムを提供することにある。   Accordingly, an object of the present invention is to provide an organic solvent treatment system for a coating chamber that pays attention to the use situation of the coating chamber and does not increase the size of the organic solvent removing device.

上記課題を解決するために、請求項1に記載の発明は、塗装及び乾燥が交互に行われる複数の塗装室に外気を除湿して供給すると共に、前記複数の塗装室で発生する有機溶剤を処理して大気中に排気する塗装室用除湿及び有機溶剤処理システムであって、前記複数の塗装室それぞれに対応して設けられ、外気を除湿して各塗装室に供給する複数の専用の除湿機と、ダクトのダンパの切換えによって、前記複数の塗装室のうち塗装が行われている塗装室に外気を除湿して供給する応援用の除湿機と、前記複数の塗装室それぞれに対応して設けられ、各塗装室で発生する有機溶剤を含む空気を処理して大気中に排気する複数の専用の有機溶剤除去装置と、ダクトのダンパの切換えによって、前記複数の塗装室のうち塗装が行われている塗装室で発生する有機溶剤を含む空気を処理して大気中に排気する応援用の有機溶剤除去装置と、を備えることを特徴とする。   In order to solve the above-mentioned problem, the invention according to claim 1 dehumidifies and supplies outside air to a plurality of coating chambers in which coating and drying are alternately performed, and an organic solvent generated in the plurality of coating chambers. A dehumidification and organic solvent treatment system for a coating chamber that treats and exhausts to the atmosphere, and is provided for each of the plurality of coating chambers, and dehumidifies the outside air and supplies it to each coating chamber A dehumidifier for supporting dehumidification and supplying the outside air to the painting chamber in which painting is performed among the plurality of painting chambers by switching the duct damper, and the plurality of painting chambers. A plurality of dedicated organic solvent removal devices that are provided and process the air containing the organic solvent generated in each coating chamber and exhaust it to the atmosphere, and by switching the duct damper, painting is performed among the plurality of coating chambers. Departure in the painting room Processing the air containing organic solvent in characterized by comprising a organic solvent remover for cheering for exhausting to the atmosphere.

請求項1に記載の発明によれば、塗装又は乾燥作業の状態に応じて、ダクトのダンパを切替えて除湿機及び有機溶剤除去装置の運転台数を制御することにより、塗装室用除湿機及び有機溶剤除去装置システムの省エネ、低価格化を図ることができる。   According to the first aspect of the present invention, by controlling the number of operating dehumidifiers and organic solvent removal devices by switching the damper of the duct according to the state of painting or drying work, Energy saving and cost reduction of the solvent removal system can be achieved.

本発明の第一の実施形態における塗装室用除湿・有機溶剤処理システムの概念図The conceptual diagram of the dehumidification and organic-solvent processing system for coating rooms in 1st embodiment of this invention 本発明の第二の実施形態における塗装室用除湿・有機溶剤処理システムの概念図The conceptual diagram of the dehumidification and organic-solvent processing system for coating rooms in 2nd embodiment of this invention 本発明の第三の実施形態における塗装室用除湿・有機溶剤処理システムの概念図The conceptual diagram of the dehumidification and organic-solvent processing system for coating rooms in 3rd embodiment of this invention 試算に用いた塗装室用除湿・有機溶剤処理システムの系統図System diagram of coating room dehumidification and organic solvent treatment system used for estimation 従来の換気システムの概念図Conceptual diagram of conventional ventilation system

以下添付図面に基づいて本発明の塗装室用除湿・有機溶剤処理システムの実施形態を説明する。図1は、本発明の第一の実施形態における塗装室用除湿・有機溶剤処理システムの概念図である。塗装室用除湿・有機溶剤処理システムは、外気を除湿して塗装室4に供給する除湿機5と、塗装室4で発生する有機溶剤を処理して大気中に排気する有機溶剤除去装置6と、を備える。   Embodiments of a dehumidification / organic solvent treatment system for a coating room according to the present invention will be described below with reference to the accompanying drawings. FIG. 1 is a conceptual diagram of a coating room dehumidification / organic solvent treatment system according to a first embodiment of the present invention. The dehumidification / organic solvent treatment system for the painting chamber includes a dehumidifier 5 that dehumidifies the outside air and supplies the dehumidification air to the painting chamber 4, and an organic solvent removal device 6 that treats the organic solvent generated in the painting chamber 4 and exhausts it to the atmosphere. .

除湿機5は、外気を除湿する除湿機本体5aと、除湿機本体5aで除湿された外気を塗装室4内へ導く吸気ダクト5bとから構成される。除湿機本体5aは、外気を冷却して水蒸気を結露させて、空気中の水分を除去する。単に冷却して結露させるだけだと相対湿度が下がるので、水分を除去した後加温することもある。冬季の湿度が低いときには加温だけのときもあるし、夏場の温度が高いときには冷却だけのときもある。除湿機本体5aの運転モードは外気の温度・湿度の条件に合わせて切り換えられる。切換えは、作業員がその日の温湿度をみて行ってもよいし、塗装室4に設置される温度・湿度センサによって自動的に行ってもよい。除湿機本体5aの処理風量、すなわち塗装室4の外気の取り入れ量は、空調便覧で定められる工場設備の換気回数0.5〜3回/hを使用するのが望ましい。   The dehumidifier 5 includes a dehumidifier body 5 a that dehumidifies outside air, and an intake duct 5 b that guides the outside air dehumidified by the dehumidifier body 5 a into the painting chamber 4. The dehumidifier body 5a cools the outside air to condense water vapor and remove moisture in the air. Relative humidity decreases simply by cooling and dew condensation, so it may be heated after removing moisture. When the humidity in winter is low, it may be only heating, and when the temperature in summer is high, it may be only cooling. The operation mode of the dehumidifier body 5a is switched according to the temperature and humidity conditions of the outside air. The switching may be performed by an operator looking at the temperature and humidity of the day, or may be automatically performed by a temperature / humidity sensor installed in the painting chamber 4. The processing air volume of the dehumidifier main body 5a, that is, the intake amount of outside air in the painting chamber 4, is preferably 0.5 to 3 times / h of factory equipment determined by the air conditioning manual.

有機溶剤除去装置6は、塗装室4内で発生する有機溶剤を処理する有機溶剤除去装置本体6aと、有機溶剤除去装置本体6aで処理された塗装室4内の空気を大気中に排気する排気ダクト6bと、排気ダクト6bから分岐し、有機溶剤除去装置本体6aで処理された塗装室4内の空気を再び塗装室4内へ循環させる循環ダクト6cと、を有する。   The organic solvent removing device 6 is an organic solvent removing device main body 6a for treating an organic solvent generated in the coating chamber 4, and an exhaust for exhausting air in the painting chamber 4 treated by the organic solvent removing device main body 6a to the atmosphere. It has a duct 6b and a circulation duct 6c that branches from the exhaust duct 6b and circulates the air in the coating chamber 4 treated by the organic solvent removing apparatus main body 6a into the coating chamber 4 again.

有機溶剤除去装置6の仕様は以下のように定められる。有機溶剤除去装置本体6aの有機溶剤の処理能力は、塗装室4内で発生する有機溶剤の発生量及び除去率(例えば90〜97%)から定められる。また、有機溶剤除去装置本体6aの処理風量は、塗装室4の容積×塗装室の換気回数(5〜8回/h)によって定められる。有機溶剤除去装置本体6aが処理した空気を大気中に排気する風量、すなわち排気ダクト6bに流れる風量は、除湿機5の処理風量に等しく設定される。また、有機溶剤除去装置本体6aが処理した空気を塗装室4内に循環させる風量、すなわち循環ダクト6cに流れる風量は、有機溶剤除去装置本体6aの全体の処理風量−排気ダクト6bに流れる風量、により求められる。   The specifications of the organic solvent removing device 6 are determined as follows. The processing capacity of the organic solvent removing device main body 6a is determined by the amount of organic solvent generated in the coating chamber 4 and the removal rate (for example, 90 to 97%). Further, the processing air volume of the organic solvent removing device main body 6a is determined by the volume of the coating chamber 4 times the number of ventilations of the coating chamber (5 to 8 times / h). The amount of air that exhausts the air treated by the organic solvent removing apparatus main body 6a into the atmosphere, that is, the amount of air flowing through the exhaust duct 6b, is set equal to the amount of air treated by the dehumidifier 5. Further, the amount of air that circulates the air treated by the organic solvent removing device main body 6a into the coating chamber 4, that is, the amount of air flowing through the circulation duct 6c, is the total amount of air flowing through the organic solvent removing device main body 6a minus the amount of air flowing through the exhaust duct 6b. Is required.

そして、求められた除湿機5の風量、有機溶剤除去装置6の風量、塗装室4内の有機溶剤の発生量、有機溶剤除去装置6の除去率等から、塗装室4内での有機溶剤の濃度を算出する。労働基準局は塗装室内での有機溶剤の濃度を100ppm以下にすることを定めている。算出された有機溶剤の濃度が100ppm以下であるかどうかを確認し、100ppm以下であれば、求められた値で除湿機5及び有機溶剤除去装置6の仕様を決定する。100ppm以上であれば、換気回数、外気取り入れ回数、有機溶剤除去装置6の除去率等を見直し、有機溶剤の濃度が100ppm以下になるまで除湿機5及び有機溶剤除去装置6の仕様を再計算する。   Then, from the obtained air volume of the dehumidifier 5, the air volume of the organic solvent removing device 6, the amount of organic solvent generated in the coating chamber 4, the removal rate of the organic solvent removing device 6, etc., the organic solvent in the coating chamber 4 Calculate the concentration. The Labor Standards Bureau stipulates that the concentration of organic solvents in the paint chamber be 100 ppm or less. It is confirmed whether or not the calculated concentration of the organic solvent is 100 ppm or less, and if it is 100 ppm or less, the specifications of the dehumidifier 5 and the organic solvent removing device 6 are determined based on the obtained values. If it is 100 ppm or more, the number of ventilations, the number of outside air intakes, the removal rate of the organic solvent removal device 6 are reviewed, and the specifications of the dehumidifier 5 and the organic solvent removal device 6 are recalculated until the concentration of the organic solvent becomes 100 ppm or less. .

この実施形態では、塗装室の大きさを例えば50m×35m×17mHに設定し、換気回数を5回/h、外気取り入れ回数を1.5回/hに設定している。この条件の下では除湿機5の風量は750m/minに、有機溶剤除去装置6の処理風量は2480m/minになる。そして、有機溶剤除去装置6が大気に排気する量は750m/minになり、塗装室4に循環させる量は1730m/minになる。同じ塗装室の大きさで算出した図5に示される従来の換気システムと比較すると、除湿機5の処理風量を2480m/minから750m/minに低減できるのがわかる。除湿機5の処理風量は、除湿機5が外気を処理する風量であり、これを約1/3に低減できると、除湿機5の容量も約1/3に低減できる。よって除湿機5が大型化するのを防ぐことができ、初期費用、ランニングコスト共に極めて低減できる。 In this embodiment, the size of the coating chamber is set to, for example, 50 m × 35 m × 17 mH, the ventilation frequency is set to 5 times / h, and the outside air intake frequency is set to 1.5 times / h. Under this condition, the air volume of the dehumidifier 5 is 750 m 3 / min, and the process air volume of the organic solvent removing device 6 is 2480 m 3 / min. And the quantity which the organic solvent removal apparatus 6 exhausts to air | atmosphere will be 750 m < 3 > / min, and the quantity circulated to the coating chamber 4 will be 1730 m < 3 > / min. Compared to conventional ventilation system shown in Figure 5 were calculated by the magnitude of the same painting chamber, the process air volume of dehumidifier 5 seen that can be reduced from 2480m 3 / min to 750m 3 / min. The processing air volume of the dehumidifier 5 is the air volume that the dehumidifier 5 processes outside air, and if this can be reduced to about 1/3, the capacity of the dehumidifier 5 can also be reduced to about 1/3. Therefore, it is possible to prevent the dehumidifier 5 from becoming large, and both initial cost and running cost can be extremely reduced.

本実施形態によれば以下の効果を奏する。有機溶剤除去装置が処理した空気の一部を塗装室に循環させるので、除湿機の処理能力を低減することができ、しかも塗装室内の有機溶剤の濃度も高くなることがない。また、大容量の塗装室からの有機溶剤排出量を完全におさえることが可能になる。さらに、有機溶剤除去装置は吸収剤としてカーボンを使用するケースが多く、このカーボンの吸湿性を利用することで、除湿機の容量を削減可能になる。   According to this embodiment, the following effects are produced. Since a part of the air processed by the organic solvent removing apparatus is circulated to the coating chamber, the processing capacity of the dehumidifier can be reduced, and the concentration of the organic solvent in the coating chamber does not increase. In addition, it is possible to completely reduce the amount of organic solvent discharged from a large-capacity coating room. Furthermore, in many cases, the organic solvent removing apparatus uses carbon as an absorbent, and the capacity of the dehumidifier can be reduced by utilizing the hygroscopicity of the carbon.

図2は、本発明の第二の実施形態における塗装室用除湿・有機溶剤処理システムを示す。この実施形態では、複数の例えば二つの塗装室7a,7bを一組にして、各塗装室7a,7bに専用の除湿機8a,8b及び専用の有機溶剤除去装置10a,10bを設けると共に、二つの塗装室7a,7bのうち塗装が行われている塗装室のみを応援にいける応援用の有機溶剤除去装置12とを設けている。応援用の有機溶剤除去装置12は、ダクトのダンパ13,14の切換えによって、二つの塗装室7a,7bのうち塗装が行われている塗装室のみの有機溶剤を含む空気を処理して当該塗装が行われている塗装室へ再び循環させる。   FIG. 2 shows a dehumidification / organic solvent treatment system for a coating chamber according to the second embodiment of the present invention. In this embodiment, a plurality of, for example, two coating chambers 7a and 7b are combined, and each coating chamber 7a and 7b is provided with a dedicated dehumidifier 8a and 8b and a dedicated organic solvent removing device 10a and 10b. A support organic solvent removing device 12 that can support only the painting chamber in which the painting is performed among the two painting chambers 7a and 7b is provided. The support organic solvent removing device 12 processes the air containing the organic solvent only in the painting chamber in which the painting is being performed out of the two painting chambers 7a and 7b by switching the dampers 13 and 14 of the duct. It is circulated again to the painting room.

作業員が塗装室7aに入り、塗装を行っているときは、換気回数が例えば5回/h必要なので、応援用の有機溶剤除去装置12が塗装室7aの有機溶剤を含む空気を処理して塗装が行われている塗装室7aへ再び循環させて5回/hを確保する。そのとき、乾燥を行っている塗装室7bでは、作業員がおらず、且つ有機溶剤の発生量も少ないので、換気回数が例えば1.5回/h程度でよい。このため、専用の有機溶剤除去装置10bのみで換気回数1.5回/hを確保する。応援用の有機溶剤除去装置12を設けて切替えることにより、除湿機と有機溶剤除去装置を合せたトータルのブロワー風量が2台×(2480m/min+2480m/min)=9920m/min必要であったところ、4台×750m/min+1730m/min=4730m/minで済む。二つの塗装室7a,7bのトータルで考えると、除湿機8a,8b及び有機溶剤除去装置10a,10b,12の風量を低減できることがわかる。 When the worker enters the painting chamber 7a and is painting, the ventilation frequency is required to be 5 times / h, for example, so the support organic solvent removing device 12 processes the air containing the organic solvent in the painting chamber 7a. It is circulated again to the painting chamber 7a where painting is performed to ensure 5 times / h. At that time, in the coating chamber 7b where drying is performed, there are no workers and the amount of organic solvent generated is small, so the ventilation frequency may be about 1.5 times / h, for example. For this reason, the ventilation frequency of 1.5 times / h is ensured only with the dedicated organic solvent removing device 10b. By providing and switching the organic solvent removing device 12 for support, the total blower air volume including the dehumidifier and the organic solvent removing device is required 2 units × (2480 m 3 / min + 2480 m 3 / min) = 9920 m 3 / min. As a result, 4 units × 750 m 3 / min + 1730 m 3 / min = 4730 m 3 / min is sufficient. Considering the total of the two coating chambers 7a and 7b, it can be seen that the air volumes of the dehumidifiers 8a and 8b and the organic solvent removing devices 10a, 10b and 12 can be reduced.

本実施形態によれば以下の効果を奏する。塗装室の除湿装置と有機溶剤除去装置との外気取り入れ、放散のバランスを、塗装・乾燥作業の状態に応じて切り換えて運転台数を制御することにより、全体システムの省エネ、低価格化を図ることができる。装置の故障等の異常時においても切り換え等で操業が可能になる。さらに、大容量の塗装室からの有機溶剤排出量を完全におさえることが可能になる。さらに、有機溶剤除去装置は吸収剤としてカーボンを使用するケースが多く、このカーボンの吸湿性を利用することで、除湿機の容量を削減可能になる。   According to this embodiment, the following effects are produced. To save energy and reduce the cost of the entire system by controlling the number of operating units by switching the balance between the intake and release of outside air between the dehumidifier and organic solvent remover in the painting room according to the state of painting and drying operations. Can do. Even when there is an abnormality such as a failure of the device, operation becomes possible by switching. Furthermore, it becomes possible to completely reduce the amount of organic solvent discharged from a large-capacity coating chamber. Furthermore, in many cases, the organic solvent removing apparatus uses carbon as an absorbent, and the capacity of the dehumidifier can be reduced by utilizing the hygroscopicity of the carbon.

図3は、本発明の第三の実施形態における塗装室用除湿・有機溶剤処理システムを示す。この実施形態でも、複数の例えば二つの塗装室14a,14bを一組にして、各塗装室14a,14bに専用の有機溶剤除去装置16a,16bを設けている。そして、ダクトのダンパの切換えによって、二つの塗装室14a,14bのうち塗装が行われている塗装室のみを応援にいける応援用の有機溶剤除去装置17を設けている。ただし、この実施形態では、応援用の有機溶剤除去装置17はダクトのダンパ19の切換えによって、二つの塗装室14a,14bのうち塗装が行われている塗装室のみの有機溶剤を含む空気を処理して大気中に排気する。除湿機15a,15bも同様に、二つの塗装室14a,14bに専用の除湿機15a,15bと、二つの塗装室14a,14bのうち塗装が行われている塗装室のみを応援にいける応援用の除湿機18と、がある。応援用の除湿機18は、ダクトのダンパ20の切り換えによって、二つの塗装室14a,14bのうち、塗装が行われている塗装室のみに外気を除湿して供給する。   FIG. 3 shows a dehumidification / organic solvent treatment system for a coating room according to a third embodiment of the present invention. Also in this embodiment, a plurality of, for example, two coating chambers 14a and 14b are set as one set, and dedicated organic solvent removing devices 16a and 16b are provided in the respective coating chambers 14a and 14b. And the organic solvent removal apparatus 17 for support which can go to support only the coating chamber in which coating is performed among the two coating chambers 14a and 14b is provided by switching the damper of a duct. However, in this embodiment, the organic solvent removal device 17 for support processes the air containing the organic solvent only in the painting chamber in which the painting is performed out of the two painting chambers 14a and 14b by switching the damper 19 of the duct. And exhaust to the atmosphere. Similarly, the dehumidifiers 15a and 15b are dedicated to supporting the two painting chambers 14a and 14b, and the dedicated dehumidifiers 15a and 15b and the painting chamber in which the painting is performed out of the two painting chambers 14a and 14b. And a dehumidifier 18. The support dehumidifier 18 dehumidifies and supplies the outside air only to the painting chamber in which painting is performed, of the two painting chambers 14a and 14b, by switching the damper 20 of the duct.

換気回数は、上記第二の実施形態における塗装室用除湿・有機溶剤処理システムと同様であり、塗装を行っている塗装室14a,14bでは換気回数の5回/hを確保し、乾燥を行っている塗装室14a,14bでは換気回数の1.5回/hを確保する。応援用の除湿機18及び応援用の有機溶剤除去装置17を設けて切替えることにより、除湿機と有機溶剤除去装置を合せたトータルのブロワー風量が2台×(2480m/min+2480m/min)=9920m/min必要であったところ、4台×750m/min+2台×1730m/min=6460m/minで済むことになる。二つの塗装室14a,14bのトータルで考えると、除湿機15a,15b,18及び有機溶剤除去装置16a,16b,17の風量を低減できることがわかる。ただし、この実施形態では上記第二の実施形態の塗装室用除湿・有機溶剤処理システムと異なり、応援用の有機溶剤除去装置17が処理した空気を循環させていないので、除湿機18の風量が上記第二の実施形態の塗装室用除湿・有機溶剤処理システムよりも大きくなってしまう。 The number of ventilations is the same as the dehumidification / organic solvent treatment system for painting rooms in the second embodiment. In the painting rooms 14a and 14b where painting is performed, the number of ventilations is 5 times / h and drying is performed. In the painting chambers 14a, 14b, the ventilation frequency of 1.5 times / h is secured. By providing and switching the support dehumidifier 18 and the support organic solvent removing device 17, the total blower air volume including the dehumidifier and the organic solvent removing device is 2 units × (2480 m 3 / min + 2480 m 3 / min) = 9920m 3 / min at was necessary, so that requires only four × 750m 3 / min + 2 units × 1730m 3 / min = 6460m 3 / min. Considering the total of the two coating chambers 14a and 14b, it can be seen that the air volumes of the dehumidifiers 15a, 15b and 18 and the organic solvent removing devices 16a, 16b and 17 can be reduced. However, in this embodiment, unlike the coating chamber dehumidification / organic solvent treatment system of the second embodiment, the air treated by the organic solvent removal device 17 for support is not circulated, so the air volume of the dehumidifier 18 is It becomes larger than the dehumidification / organic solvent treatment system for the coating chamber of the second embodiment.

本実施形態によれば以下の効果を奏する。塗装又は乾燥作業の状態に応じて、ダクトのダンパを切替えて有機溶剤除去装置の運転台数を制御することにより、有機溶剤除去装置システムの省エネ、低価格化を図ることができる。装置の故障等の異常時においても切り換え等で操業が可能になる。さらに、大容量の塗装室からの有機溶剤排出量を完全におさえることが可能になる。さらに、有機溶剤除去装置は吸収剤としてカーボンを使用するケースが多く、このカーボンの吸湿性を利用することで、除湿機の容量を削減可能になる。   According to this embodiment, the following effects are produced. By switching the damper of the duct and controlling the number of operating organic solvent removing apparatuses according to the state of painting or drying work, it is possible to save energy and reduce the cost of the organic solvent removing apparatus system. Even when there is an abnormality such as a failure of the device, operation becomes possible by switching. Furthermore, it becomes possible to completely reduce the amount of organic solvent discharged from a large-capacity coating chamber. Furthermore, in many cases, the organic solvent removing apparatus uses carbon as an absorbent, and the capacity of the dehumidifier can be reduced by utilizing the hygroscopicity of the carbon.

第二の実施形態の塗装室用除湿・有機溶剤処理システムを用いて、塗装室の換気量・循環量と室内の有機溶剤の濃度を試算した。具体的には、表1及び図4に示されるように、塗装室の容積×換気回数、で全体の換気風量を求めた。次に外気取入れ回数を定め、専用の除湿機及び専用の有機溶剤除去装置の風量を求め、全体の換気風量−専用の有機溶剤除去装置の風量、から応援用の有機溶剤除去装置の風量を求めた。図4中左側が塗装を行っている塗装室であり、換気回数を5回/hにとっている。右側が乾燥を行っている塗装室であり、換気回数を1.5回/hにとっている。この条件のもと、有機溶剤除去装置の除去率から塗装室内の有機溶剤の濃度を求めた。その結果、塗装室内の有機溶剤の濃度を100ppm以下に低減できることがわかった。   Using the coating room dehumidification / organic solvent treatment system of the second embodiment, the ventilation volume / circulation rate of the coating room and the concentration of the organic solvent in the room were estimated. Specifically, as shown in Table 1 and FIG. 4, the entire ventilation air volume was obtained by the volume of the painting chamber × the number of ventilations. Next, determine the number of outside air intakes, determine the air volume of the dedicated dehumidifier and the dedicated organic solvent removal device, and calculate the air volume of the support organic solvent removal device from the overall ventilation air flow-the volume of the dedicated organic solvent removal device. It was. The left side in FIG. 4 is a painting room where painting is performed, and the ventilation frequency is set to 5 times / h. The painting room on the right side is drying, and the ventilation frequency is 1.5 times / h. Under these conditions, the concentration of the organic solvent in the coating chamber was determined from the removal rate of the organic solvent removing device. As a result, it was found that the concentration of the organic solvent in the coating chamber can be reduced to 100 ppm or less.

Figure 0005386008
Figure 0005386008

4…塗装室
5…除湿機
6…有機溶剤除去装置
7a,7b…塗装室
8a,8b…専用の除湿機
10a,10b…専用の有機溶剤除去装置
12…応援用の有機溶剤除去装置
13,14…ダンパ
14a,14b…塗装室
15a,15b…専用の除湿機
16a,16b…専用の有機溶剤除去装置
17…応援用の有機溶剤除去装置
18…応援用の除湿機
19…ダンパ

20…ダンパ
4 ... Painting room 5 ... Dehumidifier 6 ... Organic solvent removing devices 7a, 7b ... Painting chambers 8a, 8b ... Dedicated dehumidifiers 10a, 10b ... Dedicated organic solvent removing device 12 ... Supporting organic solvent removing devices 13,14 ... Dampers 14a, 14b ... Painting chambers 15a, 15b ... Dedicated dehumidifiers 16a, 16b ... Dedicated organic solvent removal device 17 ... Support organic solvent removal device 18 ... Support dehumidifier 19 ... Damper

20 ... Damper

Claims (1)

塗装及び乾燥が交互に行われる複数の塗装室に外気を除湿して供給すると共に、前記複数の塗装室で発生する有機溶剤を処理して大気中に排気する塗装室用除湿及び有機溶剤処理システムであって、
前記複数の塗装室それぞれに対応して設けられ、外気を除湿して各塗装室に供給する複数の専用の除湿機と、
ダクトのダンパの切換えによって、前記複数の塗装室のうち塗装が行われている塗装室に外気を除湿して供給する応援用の除湿機と、
前記複数の塗装室それぞれに対応して設けられ、各塗装室で発生する有機溶剤を含む空気を処理して大気中に排気する複数の専用の有機溶剤除去装置と、
ダクトのダンパの切換えによって、前記複数の塗装室のうち塗装が行われている塗装室で発生する有機溶剤を含む空気を処理して大気中に排気する応援用の有機溶剤除去装置と、を備えることを特徴とする塗装室用除湿及び有機溶剤処理システム。
A dehumidification and organic solvent treatment system for a coating chamber that dehumidifies and supplies outside air to a plurality of coating chambers in which painting and drying are alternately performed, and processes organic solvents generated in the plurality of coating chambers to exhaust them to the atmosphere. Because
A plurality of dedicated dehumidifiers provided corresponding to each of the plurality of coating chambers, dehumidifying the outside air and supplying each coating chamber;
A dehumidifier for support that dehumidifies and supplies outside air to the painting chamber where the painting is performed among the plurality of painting chambers by switching the damper of the duct,
A plurality of dedicated organic solvent removal devices that are provided corresponding to each of the plurality of coating chambers, process air containing an organic solvent generated in each coating chamber, and exhaust the air into the atmosphere;
A support organic solvent removing device that processes air containing an organic solvent generated in a painting chamber in which painting is performed among the plurality of painting chambers by switching a duct damper, and exhausts the air into the atmosphere. A dehumidification and organic solvent treatment system for a painting room.
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JP2004036908A (en) * 2002-06-28 2004-02-05 Nissan Motor Co Ltd Baking finish drying furnace
JP4188654B2 (en) * 2002-10-03 2008-11-26 三菱電機株式会社 Air conditioner
JP4051014B2 (en) * 2003-09-11 2008-02-20 アンデックス株式会社 painting booth

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