JPS62277174A - Painting booth - Google Patents

Painting booth

Info

Publication number
JPS62277174A
JPS62277174A JP61120757A JP12075786A JPS62277174A JP S62277174 A JPS62277174 A JP S62277174A JP 61120757 A JP61120757 A JP 61120757A JP 12075786 A JP12075786 A JP 12075786A JP S62277174 A JPS62277174 A JP S62277174A
Authority
JP
Japan
Prior art keywords
heat
cleaning liquid
cleaning
painting
paint mist
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP61120757A
Other languages
Japanese (ja)
Inventor
Koji Morioka
森岡 宏次
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Taikisha Ltd
Original Assignee
Taikisha Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Taikisha Ltd filed Critical Taikisha Ltd
Priority to JP61120757A priority Critical patent/JPS62277174A/en
Publication of JPS62277174A publication Critical patent/JPS62277174A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To recover the waste heat from a painting operation area and to reduce an energy loss by evaporating the cleaning liquid after cleaning in a paint mist removing device and subjecting the evaporated cleaning liquid and a heat medium for recovering heat to a heat exchanger. CONSTITUTION:The painting scum of the cleaning liquid W after said liquid is used for the cleaning operation from the paint mist removing device of a booth for painting automobile bodies, castings of electrical household appliances, etc., is separated and is supplied to a heat exchanger 24. The heat exchanger 24 is provided with a carbureter part to evaporate the cleaning water W and a condenser part to deprive the evaporated water W of the condensation heat. The circulating heat medium liquid of a preheating coil 16 of an air conditioner 3 and the evaporated cleaning liquid W are subjected to the heat exchange by the heat exchanger 31 in the condenser part. The waste heat from the painting operation area is thus extremely satisfactorily recovered with high efficiency for a long period of time, by which the energy loss is additionally effectively reduced.

Description

【発明の詳細な説明】 3、発明の詳細な説明 〔産業上の利用分野〕 本発明は、自動車ボディーや家電製品のケーシング等を
塗装するための塗装ブースに関し、詳しくは、塗装作業
域への供給換気気体を温調する空調器、及び、前記塗装
作業域からの排気気体と洗浄液とを接触させて排気気体
中の塗料ミストを捕捉除去する塗料ミスト除去装置を備
えた塗装ブースに関する。
[Detailed Description of the Invention] 3. Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a painting booth for painting automobile bodies, casings of home appliances, etc. The present invention relates to a painting booth equipped with an air conditioner that controls the temperature of supplied ventilation gas, and a paint mist removal device that captures and removes paint mist in the exhaust gas by bringing the exhaust gas from the painting work area into contact with a cleaning liquid.

〔従来の技術〕[Conventional technology]

従来、上記の如き塗装ブースにおいて塗装作業域から排
気気体とともに系外に持ち出される排熱を回収してエネ
ルギーロスを抑制するには、塗料ミスト除去装置におい
て洗浄液を循環使用するようにした上で、第5図に示す
ように、塗料ミスト除去装置(8)を通過した後の排気
気体と空調器(3)への取入外気とを熱交換させて取大
外気を予熱する全熱交換器(36)を設けたり、又、第
6図に示すように、塗料ミスト除去装置(8)を通過し
た後の排気気体を受熱源とするヒートポンプ(35)を
設けて、そのヒートポンプ(35)により空調器(3)
の温調コイル(16)に対する熱媒液を加熱する等して
いた。
Conventionally, in order to suppress energy loss by recovering the waste heat carried out of the system together with the exhaust gas from the painting work area in the above-mentioned painting booth, the cleaning solution was circulated in the paint mist removal device, and then As shown in Figure 5, there is a total heat exchanger (1) that preheats the outside air taken in by exchanging heat between the exhaust gas that has passed through the paint mist removal device (8) and the outside air taken into the air conditioner (3). 36), or, as shown in Figure 6, a heat pump (35) is installed that uses the exhaust gas that has passed through the paint mist removal device (8) as a heat receiving source, and the heat pump (35) performs air conditioning. Vessel (3)
The heating medium liquid for the temperature control coil (16) was heated.

つまり、塗装作業域からの排熱を回収するには塗料ミス
ト除去装置通過以前の排気気体からその保有熱量を回収
することが最も直接的ではあるが、塗料ミスト除去装置
において洗浄液を循環ポンプにより循環使用するように
すれば、定常運転状態において循環洗浄液は、排気気体
との接触のために塗装作業域内の換気気体露点温度に限
りなく近づいた温度となって平衡状態に達し、そのため
に、塗装作業域からの排熱は、塗料ミスト除去装置通過
後も排気気体保有熱量としてその大部分が排気気体に保
有されたままで排出されることとなる。
In other words, the most direct way to recover waste heat from the painting work area is to recover the amount of heat retained in the exhaust gas before it passes through the paint mist removal device, but in the paint mist removal device, the cleaning fluid is circulated using a circulation pump. If used, under steady-state operating conditions, the circulating cleaning fluid will reach an equilibrium state due to contact with the exhaust gas, with a temperature as close as possible to the ventilation gas dew point temperature in the painting work area, thus preventing the painting work from occurring. Even after passing through the paint mist removal device, most of the exhaust heat from the area remains retained in the exhaust gas as the amount of heat retained in the exhaust gas.

すなわち、塗料ミスト除去装置通過後の排気気体からで
も十分な熱回収が可能となり、又、塗料ミスト除去装置
通過後の排気気体であれば塗料ミストも除去されていて
排熱回収用熱交換器に対する塗料ミストの付着・堆積も
抑制できるという観点から、前述の如く、塗料ミスト除
去装置を通過した後の排気気体と排熱回収用熱媒(取入
外気や温調コイルに対する熱媒液等)とを熱交換させて
排熱を回収するようにしていた(文献を示すことができ
ない)。
In other words, sufficient heat can be recovered even from the exhaust gas that has passed through the paint mist removal device, and paint mist has also been removed from the exhaust gas that has passed through the paint mist removal device, making it possible to recover sufficient heat from the exhaust gas that has passed through the paint mist removal device. From the viewpoint of suppressing adhesion and accumulation of paint mist, as mentioned above, the exhaust gas after passing through the paint mist removal device and the heat medium for exhaust heat recovery (heat medium liquid for intake outside air, temperature control coil, etc.) The waste heat was recovered by exchanging heat (I can't provide any literature).

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかし、洗浄液との接触による塗料ミスト除去処理を施
すものの塗料ミスト除去装置通過後の排気気体には未だ
かなりの量の細かい塗料ミストが残るものであり、フィ
ルター等により残った塗料ミストを極力除去するにして
も、排気気体中に残った塗料ミストがその高い粘着性に
より排熱回収用熱交換器(対取人外気用の全熱交換器や
ヒートポンプの受熱側熱交換器等)に付着堆積し、その
ために、熱交換効率(すなわち、排熱回収効率)が大巾
に低下して十分な排熱1回収が達成できなくなる問題が
あった。
However, even though the paint mist is removed by contact with the cleaning liquid, a considerable amount of fine paint mist still remains in the exhaust gas after passing through the paint mist removal device. However, due to its high stickiness, the paint mist remaining in the exhaust gas can adhere to and accumulate on exhaust heat recovery heat exchangers (total heat exchangers for external air, heat exchangers on the heat receiving side of heat pumps, etc.). Therefore, there is a problem in that the heat exchange efficiency (that is, the exhaust heat recovery efficiency) decreases significantly, making it impossible to achieve sufficient exhaust heat recovery.

本発明の目的は、排熱回収を排気気体から直接に行うと
いう従来の考え方を脱し、排気気体と洗浄液との接触に
よる塗料ミスト除去処理に着目した合理的な排熱回収に
より、塗料ミストの付着堆積に起因した排熱回収効率の
低下を効果的に回避し、併せて、排熱回収効率そのもの
の一層の向上を図ると共に排熱回収構成の小型化をも図
る点にある。
The purpose of the present invention is to move away from the conventional concept of recovering exhaust heat directly from exhaust gas, and to eliminate the adhesion of paint mist through rational exhaust heat recovery that focuses on removing paint mist through contact between exhaust gas and cleaning fluid. The object of the present invention is to effectively avoid a decrease in exhaust heat recovery efficiency due to deposition, further improve the exhaust heat recovery efficiency itself, and downsize the exhaust heat recovery structure.

〔問題点を解決するための手段〕[Means for solving problems]

本発明による塗装ブースの特徴構成は、温調換気気体供
給を受ける塗装作業域からの排気気体と洗浄液とを接触
させて排気気体中の塗料ミストを除去する塗料ミスト除
去装置を備えた構成において、その塗料ミスト除去装置
で洗浄作用した後の洗浄液を蒸発させるための低圧空間
を形成する気化器を設け、その気化器において蒸発した
気化洗浄液と熱回収用熱媒とを熱交換させて気化洗浄液
から凝縮熱を奪うことにより前記塗装作業域からの排熱
を回収する熱交換器を設けたことにあり、その作用・効
果は次の通りである。
The characteristic configuration of the painting booth according to the present invention is that it is equipped with a paint mist removal device that removes paint mist from the exhaust gas by bringing the exhaust gas from the painting work area supplied with temperature-controlled ventilation gas into contact with the cleaning liquid. A vaporizer is installed to form a low-pressure space for evaporating the cleaning liquid after the cleaning action has been performed by the paint mist removal device, and the vaporized cleaning liquid is exchanged with the heat recovery heat medium in the vaporizer to remove the vaporized cleaning liquid. A heat exchanger is provided to recover waste heat from the painting area by removing condensation heat, and its functions and effects are as follows.

〔作 用〕[For production]

つまり、塗料ミスト除去のための排気気体と洗浄液との
接触を、排気気体から洗浄液へ排熱授与させる直接熱交
換に利用し、その直接熱交換により洗浄液へ授与された
排熱を洗浄液と熱回収用熱媒体との熱交換をもって洗浄
液から回収するのである。
In other words, the contact between the exhaust gas and the cleaning liquid for paint mist removal is used for direct heat exchange in which the exhaust gas transfers waste heat to the cleaning liquid, and the exhaust heat transferred to the cleaning liquid through the direct heat exchange is recovered with the cleaning liquid. It is recovered from the cleaning liquid through heat exchange with the heat transfer medium.

その際、洗浄作用後の洗浄液には排気気体から捕捉した
塗料滓が含まれるが、気化器の低圧空間おいて洗浄液を
蒸発させ、その蒸発した気化洗浄液と熱回収用熱媒との
熱交換で気化洗浄液の凝縮熱を熱回収熱媒に与えて排熱
を回収するから、すなわち、洗浄液をいったん気化させ
てその気化洗浄液から排熱を回収するから、洗浄液中の
塗料滓が熱交換器に付着することは極めて効果的に回避
される。
At that time, the cleaning liquid after the cleaning action contains paint slag captured from the exhaust gas, but the cleaning liquid is evaporated in the low-pressure space of the vaporizer, and heat exchange between the evaporated vaporized cleaning liquid and the heat recovery heat medium is performed. Since the condensation heat of the vaporized cleaning liquid is given to the heat recovery heat medium and the waste heat is recovered, in other words, the cleaning liquid is once vaporized and the waste heat is recovered from the vaporized cleaning liquid, so paint slag in the cleaning liquid will adhere to the heat exchanger. This is very effectively avoided.

しかも、熱回収用熱媒として取入外気等の気体を対象と
する場合、従来の型式であれば気体対気体の熱交換とな
るのに対し本発明によれば気体対低圧気化液体の熱交換
となり、又、熱回収用熱媒として熱媒液を対象とする場
合、従来の型式であれば液体対気体となるのに対し本発
明によれば液体対低圧気化液体の熱交換となることから
、熱回収用熱媒が気体の場合、及び、液体の場合のいず
れにおいても、夫々、従来の型式よりも熱交換効率その
ものを向上できると共に熱交換構成を小型化できる。
Furthermore, when using a gas such as intake outside air as a heating medium for heat recovery, the conventional method involves gas-to-gas heat exchange, but according to the present invention, heat exchange occurs between gas and low-pressure vaporized liquid. In addition, when using a heat medium liquid as a heat medium for heat recovery, the heat exchange is between liquid and gas in the conventional type, but according to the present invention, heat exchange is between liquid and low-pressure vaporized liquid. Regardless of whether the heat recovery medium is a gas or a liquid, the heat exchange efficiency itself can be improved and the heat exchange configuration can be downsized compared to conventional types.

尚、上述の各作用は、塗料ミスト除去装置において洗浄
液を一過的に消費する型式、及び、循環使用する型式の
いずれの場合にも現出され、循環使用する型式の場合に
は洗浄作用後の洗浄液から排熱を回収することで循環洗
浄液と排気気体との直接熱交換による排熱授受が継続さ
れる。
The above-mentioned effects occur in both types of paint mist removal equipment, such as those that temporarily consume the cleaning liquid and those that use it recirculatingly. By recovering exhaust heat from the cleaning fluid, the exchange of exhaust heat through direct heat exchange between the circulating cleaning fluid and the exhaust gas continues.

〔発明の効果〕〔Effect of the invention〕

上述の結果、塗装作業域からの排熱を高効率で長期にわ
たって極めて良好に回収できて従来装置に較ベエネルギ
ーロスを一層効果的に低減できるようになり、ひいては
、ランニングコストの大巾な節減を達成できた。
As a result of the above, waste heat from the painting area can be recovered with high efficiency over a long period of time, making it possible to more effectively reduce energy loss compared to conventional equipment, and in turn, significantly reducing running costs. I was able to achieve this.

又、熱交換構成の小型化により塗装ブースの設置性を向
上でき、塗装工場等でのスペースの有効利用の面でも有
利となった。
Furthermore, by making the heat exchanger structure more compact, the ease of installing the paint booth can be improved, which is also advantageous in terms of effective use of space in paint factories and the like.

〔第1実施例〕 次に本発明の第1実施例を説明する。[First example] Next, a first embodiment of the present invention will be described.

第1図は塗装ブースの全体構成を示し、塗装ロボット(
1)を装備した塗装作業域(2)の天井部に、空調器(
3)からの温調換気空気を下方向きに吹出す吹出口(4
)を設けると共に、床部を格子構成の排気口(5)に形
成し、吹出口(4)からの換気空気供給に伴い、作業域
(2)内の余剰吹付塗料ミストを域内空気とともに排気
口(5)から排出するようにしである。
Figure 1 shows the overall configuration of the painting booth, and shows the painting robot (
An air conditioner (
Air outlet (4) that blows out the temperature-controlled ventilation air from (3) downward.
), and the floor is formed with a lattice-structured exhaust port (5), and as ventilation air is supplied from the outlet (4), excess spray paint mist in the work area (2) is removed together with the air within the area. It should be discharged from (5).

図中(A)は被塗物がある。In the figure (A) there is an object to be coated.

格子構成の床部の下方に、落下塗料塊、並びに、作業域
(2)からの排気空気を受止める洗浄水流下槽(6)を
設けると共に、その洗浄水流下槽(6)からの溢水と排
気空気とを攪拌状態で高速流下させる屈曲絞り流路(7
ンを設け、もって、排気空気と洗浄水(W)とを接触さ
せることにより排気空気中の塗料ミストを捕捉除去する
塗料ミスト除去装置(8)を構成しである。
A cleaning water flow tank (6) is provided below the floor with a grid structure to catch fallen paint lumps and exhaust air from the work area (2), and also to prevent overflow from the cleaning water flow tank (6). A curved constriction channel (7
This constitutes a paint mist removal device (8) that captures and removes paint mist in the exhaust air by bringing the exhaust air into contact with cleaning water (W).

塗料ミスト除去装置(8)を通過した排気空気は排気フ
ァン(9)を介して系外に排出される。
The exhaust air that has passed through the paint mist removal device (8) is exhausted to the outside of the system via an exhaust fan (9).

図中(10)は屈曲絞り流路(7)からの流下洗浄水を
受止める水槽であり、その水槽(10)に受止められた
洗浄水(W)は、塗料滓分離器(11)、並びに、分離
塗料滓掻取り器(12)を備えた貯留槽(13)に供給
されて浄化された後、循環ポンプク27)により再び洗
浄水流下槽(6)に循環供給される。
In the figure, (10) is a water tank that receives the washing water flowing down from the bent constriction channel (7), and the washing water (W) received in the water tank (10) is transferred to the paint slag separator (11), Further, after being supplied to a storage tank (13) equipped with a separation paint sludge scraper (12) and purified, it is again circulated and supplied to the washing water lower tank (6) by a circulation pump 27).

一方、空調器(3)は、プレフィルタ−(15)、予熱
コイル(16)、加湿器(17)、冷却コイル(18)
、及び再熱コイル(19)を内装しており、外気取入口
(20)から取入れた外気は空調器(3)で除塵処理、
温調処理、並びに、湿度調整処理を施された後、換気空
気として給気ファン(21)により吹出口(4)に供給
される。
On the other hand, the air conditioner (3) includes a prefilter (15), a preheating coil (16), a humidifier (17), and a cooling coil (18).
, and a reheating coil (19), and the outside air taken in from the outside air intake (20) is treated with dust removal by the air conditioner (3).
After being subjected to temperature control processing and humidity control processing, it is supplied as ventilation air to the outlet (4) by the air supply fan (21).

図中(22)は冷却コイル(18)に対して冷水やブラ
イン等の低温冷媒を循環供給する冷熱源装置であり、又
、(23)は再熱コイル(19)に対して温水や蒸気等
の高温熱媒を循環供給する温熱源装置である。
In the figure, (22) is a cold heat source device that circulates and supplies low-temperature refrigerant such as cold water or brine to the cooling coil (18), and (23) is a cold heat source device that supplies hot water, steam, etc. to the reheating coil (19). This is a heat source device that circulates and supplies high-temperature heat medium.

又、この塗装ブースにおいては、塗装作業域(2)から
排気空気とともに持ち出される排熱を回収して、その回
収熱量を空調用熱量の一部として再利用することで、排
熱ロスを抑制して空調に要するエネルギーの節減を図る
ようにしてあり、その具体的排熱回収構成としては、洗
浄水(W)の蒸発・凝縮を利用して洗浄水(W)の保有
熱量を汲み上げる熱交換装置(24)を設け、洗浄水貯
留槽(13)において塗料滓分離器(11)よりも下流
側から洗浄水(W)を取出して、その取出洗浄水(−)
を熱交換装置(24)に供給するポンプ(25)を設け
、一方、洗浄水(W)から汲み上げた熱量をもって空調
器(3)の予熱コイノ喧16)に対する循環熱媒液を加
熱するように、予熱コイル(16)に対する熱媒循環路
(26)に熱交換装置(24)を介装している。
In addition, in this painting booth, exhaust heat loss is suppressed by recovering the exhaust heat taken out with the exhaust air from the painting work area (2) and reusing the recovered heat as part of the heat for air conditioning. The system is designed to reduce the energy required for air conditioning, and the specific exhaust heat recovery structure is a heat exchange device that pumps up the heat retained in the wash water (W) by using the evaporation and condensation of the wash water (W). (24) is provided, and the cleaning water (W) is taken out from the downstream side of the paint slag separator (11) in the cleaning water storage tank (13), and the extracted cleaning water (-)
A pump (25) is provided to supply water to the heat exchanger (24), and on the other hand, the amount of heat pumped up from the wash water (W) is used to heat the circulating heat medium liquid for the preheating unit 16) of the air conditioner (3). A heat exchange device (24) is interposed in the heat medium circulation path (26) for the preheating coil (16).

つまり、塗料ミスト除去装置(8)における排気空気と
洗浄水(W)との接触を、排気空気から洗浄水先)へ排
熱授与させる直接交換に利用し、その直接熱交換により
洗浄水(W)へ授与された排熱を熱交換装置(24)で
汲み上げ、その汲み上げ排熱を熱源として空調器(3)
への取入外気を予熱するようにしである。
In other words, the contact between the exhaust air and the cleaning water (W) in the paint mist removal device (8) is used for direct exchange of exhaust heat from the exhaust air to the cleaning water tip. The heat exchanger (24) pumps up the waste heat given to the air conditioner (3) using the pumped waste heat as a heat source.
This is to preheat the outside air taken in.

熱交換装置(24)において保有排熱を予熱コイル(1
6)の循環熱媒液に授与した後の洗浄水先)は、ポンプ
(27)により再び洗浄水流下槽(6)に供給される。
In the heat exchanger (24), the retained waste heat is transferred to the preheating coil (1
The cleaning water flow after being applied to the circulating heat transfer liquid in step 6) is again supplied to the cleaning water flow lower tank (6) by the pump (27).

熱交換装置(24)は機能上、洗浄水(匈)を蒸発させ
る気化器部分とその蒸発した気化洗浄水(イ)から凝縮
熱を奪取する凝縮器部分とを備えており、気化器部分の
構成としては、底部を洗浄水溜り部とする密閉容器(2
8)を設け、その密閉容器(28)内を洗浄水蒸発用の
低圧空間とする真空ポンプ(29)を設け、更に、洗浄
水貯留槽(13)からの供給洗浄水(−)を低圧空間内
で噴水状に溢れ出させる噴出器(30)を設けである。
The heat exchange device (24) is functionally equipped with a vaporizer part that evaporates the cleaning water (X) and a condenser part that takes condensation heat from the evaporated vaporized cleaning water (A). The structure consists of an airtight container (2
8), and a vacuum pump (29) that makes the inside of the closed container (28) a low-pressure space for evaporating the washing water, and furthermore, a vacuum pump (29) is provided to make the inside of the sealed container (28) a low-pressure space for evaporating the washing water (-) from the washing water storage tank (13). A spout (30) is provided to cause the water to overflow in the form of a fountain.

又、凝縮器部分の構成としては、空調器(3)の予熱コ
イル(16)に対する循環熱媒液を管路内流動させるに
伴い、その循環熱媒と気化洗浄液(−)を熱交換させる
熱交換器(31)を密閉容器(28)内の上部に配設し
である。
In addition, as for the configuration of the condenser part, as the circulating heat medium liquid flows in the pipe for the preheating coil (16) of the air conditioner (3), heat is exchanged between the circulating heat medium and the vaporized cleaning liquid (-). The exchanger (31) is disposed in the upper part of the closed container (28).

つまり、低圧空間内で洗浄水先)を噴出させることで洗
浄水(−)を蒸発気化させて、その気化洗浄水(W)を
熱媒液との熱交換で凝縮させることにより、その際の凝
縮熱を熱媒液に授与するようにしである。
In other words, the cleaning water (-) is evaporated by ejecting the cleaning water tip in a low-pressure space, and the vaporized cleaning water (W) is condensed by heat exchange with the heat transfer liquid. This is to impart heat to the heat transfer liquid.

尚、洗浄水(W)の蒸発・凝縮を利用して洗浄水(W)
から排熱を回収するようにしたことで、たとへ貯留槽(
13)から熱交換装置(24)へ供給される洗浄水(W
)に塗料滓分離器(11)を通過した微細な塗料粒子が
含まれていたとしても、その塗料粒子の熱交換器(31
)に対する付着・堆積はほぼ確実に防止され、熱交換器
(31)の熱効果効率、すなわち、排熱回収効率は極め
て高く維持される。
In addition, using the evaporation and condensation of the washing water (W), the washing water (W)
By recovering exhaust heat from the Totohe storage tank (
Washing water (W) supplied from 13) to the heat exchanger (24)
) contains fine paint particles that have passed through the paint slag separator (11), the paint particle heat exchanger (31)
) is almost certainly prevented, and the thermal efficiency of the heat exchanger (31), that is, the exhaust heat recovery efficiency, is maintained at an extremely high level.

図中(32)はエリミネータである。In the figure (32) is an eliminator.

本例においては、空調器(3)内の取入外気流動経路に
おいて予熱コイル(16)を加湿器(17)よりも上流
側に配設したが、予熱コイル(16)を加湿器(17)
より下流側に配設して加湿器(17)からの噴霧水を予
熱コイル(16)に吹き付けるようにすることで、予熱
コイル(16)で顕熱交換のみならず潜熱交換をも行わ
せるようにし、それによって、予熱コイル(16)の総
括伝熱係数を大きくして排熱利用効率の向上、並びに、
予熱コイル(16)の小型化を図ると共に、気化洗浄水
を凝縮させる熱交換器(31)での有効温度差を大きく
採れるようにして排熱回収効率の一層の向上と、並びに
、その熱交換器(31)の小型化を図るようにしても良
い。
In this example, the preheating coil (16) is placed upstream of the humidifier (17) in the intake outside air flow path in the air conditioner (3).
By arranging the humidifier (17) further downstream and spraying the spray water from the humidifier (17) onto the preheating coil (16), the preheating coil (16) can perform not only sensible heat exchange but also latent heat exchange. By doing so, the overall heat transfer coefficient of the preheating coil (16) is increased to improve waste heat utilization efficiency, and
In addition to downsizing the preheating coil (16), the heat exchanger (31) that condenses the vaporized cleaning water can have a large effective temperature difference, thereby further improving the exhaust heat recovery efficiency and improving the heat exchange. The container (31) may be made smaller.

又、予熱コイル(16)において顕熱交換と潜熱交換と
の両方を行わせる場合、加湿用水を予熱コイル(16)
に吹き付ける構成に代えて、加湿用水を予熱コイル(1
6)に滴下するような構成としても良い。
In addition, when both sensible heat exchange and latent heat exchange are performed in the preheating coil (16), the humidifying water is transferred to the preheating coil (16).
Instead of spraying humidifying water onto a preheating coil (1
6) may be configured such that it is dropped.

〔第2実施例〕 次に本発明の第2実施例を説明する。[Second example] Next, a second embodiment of the present invention will be described.

前述第1実施例で説明した第1図に示す如き構成とほぼ
同構成の塗装ブースにおいて、洗浄水(W)の蒸発・凝
縮を利用して洗浄水艶)の保有熱量(すなわち、塗装作
業域(2)からの排熱)を回収する熱交換装置(24)
を構成するに、第2図に示すように、下部筒胴型容器(
28A)に洗浄水噴霧器(30)を内装して気化器を構
成すると共に、その気化器側の下部筒胴型容器(28A
)に連通ずる上部筒胴型容器(28B)に熱交換器(3
1)を内装して凝縮器を構成し、それら気化器と凝縮器
との対から成る熱交換ユニットの複数(24A)。
In a painting booth having almost the same configuration as the one shown in FIG. 1 explained in the first embodiment, the evaporation and condensation of the cleaning water (W) is used to reduce the amount of heat retained in the cleaning water (W) (i.e., in the painting work area). (2) Heat exchange device (24) that recovers waste heat from
As shown in Fig. 2, the lower cylindrical container (
28A) is equipped with a cleaning water sprayer (30) to form a vaporizer, and the lower cylindrical container (28A) on the vaporizer side is
) A heat exchanger (3
1) to constitute a condenser, and a plurality of heat exchange units (24A) each consisting of a pair of a vaporizer and a condenser.

(24B) 、 (24C)を、それらユニ・ソト(2
4A) 、 (24B) 。
(24B) and (24C), and their Uni-Soto (2
4A), (24B).

(24C)の気化器どうしを洗浄水供給経路において直
列に接続して、かつ、それらユニット(24A) 。
The vaporizers of (24C) are connected in series in the wash water supply path, and these units (24A).

(24B) 、 (24C)の凝縮器側熱交!#、器(
31)どうしを空調器(3)の予熱コイル(16)に対
する熱媒循環経路(26)において直列に接続して並設
し、更に、各ユニット(24A) 、 (24B) 、
 (24C)の上部筒胴型容器(28B)の夫々に対し
て真空ポンプ(29)を接続しである。
(24B), (24C) condenser side heat exchange! #,vessel(
31) The units are connected in series and arranged in parallel in the heat medium circulation path (26) for the preheating coil (16) of the air conditioner (3), and each unit (24A), (24B),
A vacuum pump (29) is connected to each of the upper cylindrical containers (28B) of (24C).

つまり、塗料ミスト除去装置(8)での排気空気との接
触により塗装作業域(2)からの排熱を授与された洗浄
水(W)の気化器内の低圧空間で蒸発させ、かつ、その
蒸発した気化洗浄水(W)を凝縮器内の熱交換器(31
)で凝縮させて、その際の凝縮熱を予熱コイル(16)
に対する循環熱媒液に与えるという形態す排熱回収を多
段で実施し、それによって、排熱回収量の増大を図るよ
うにしである。
That is, the exhaust heat from the painting work area (2) is evaporated in the low-pressure space in the vaporizer of the washing water (W) given by contact with the exhaust air in the paint mist removal device (8), and The evaporated cleaning water (W) is transferred to the heat exchanger (31) in the condenser.
), and the condensation heat is transferred to the preheating coil (16).
The exhaust heat recovery is carried out in multiple stages by giving it to the circulating heat transfer liquid, thereby increasing the amount of exhaust heat recovery.

尚、直列的に並設した熱交換ユニッ) (24A) 。In addition, heat exchange units (24A) were installed in parallel in series.

(24B) 、 (24C>に対する、洗浄水(W)の
流れ方向と予熱コイル用循環熱媒液(W)の流れ方向と
は互いに逆向きにしてあり、いわゆる対向流型式の熱交
換形態を採用することで、各熱交換器(31)の熱交換
効率、すなわち、排熱回収効率の一層の向上を図るよう
にしである。
(24B), (24C>, the flow direction of the cleaning water (W) and the flow direction of the circulating heat medium liquid (W) for the preheating coil are opposite to each other, and a so-called counterflow type heat exchange form is adopted. By doing so, the heat exchange efficiency of each heat exchanger (31), that is, the exhaust heat recovery efficiency is further improved.

〔その他の実施例〕[Other Examples]

次にその他の実施例を列記する。 Next, other examples will be listed.

第3図に示すように、塗料ミスト除去装置(8)で洗浄
作用した後の洗浄液(W)を低圧空間で蒸発させる気化
器構成として、真空ポンプ(29)に接続した容器(2
8)に洗浄液撒布ノズル(33)を内装し、一方、気化
洗浄液(W)を熱回収用熱媒とを熱交換させる構成とし
て、気化洗浄液(W)を管路内流動させるチューブ型熱
交換器(31)を空調器(3)への外気取入風路(34
)に介装し、もって、気化洗浄液(W)と取入外気との
熱交換により、管路内流動に伴い気化洗浄液(W)を概
縮させる状態で洗浄液(−)の保有排熱を取入外気に与
えるようにしても良い。
As shown in Fig. 3, a container (2) connected to a vacuum pump (29) is used as a vaporizer to evaporate the cleaning liquid (W) in a low-pressure space after being cleaned by the paint mist removal device (8).
8) is equipped with a cleaning liquid spraying nozzle (33), and on the other hand, a tube-type heat exchanger that allows the vaporized cleaning liquid (W) to flow through the pipes so as to exchange heat between the vaporized cleaning liquid (W) and a heat medium for heat recovery. (31) to the outside air intake path (34) to the air conditioner (3).
), and by heat exchange between the vaporized cleaning liquid (W) and the intake outside air, the retained waste heat of the cleaning liquid (-) is removed while the vaporized cleaning liquid (W) is compressed as it flows in the pipe. It is also possible to provide air in and out.

又、第4図に示すように、空調器(3)で用いる空調用
熱媒を加熱するヒートポンプ(35)を設けると共に、
洗浄液(W)を蒸発させる低圧空間を形成する容器(2
8)に対して、そのヒートポンプ(35)の受熱側熱交
換器(31)を内装し、もって、ヒートポンプ(35)
の作動熱媒と気化洗浄液(譬)との熱交換で気化洗浄液
(W)を凝縮させて洗浄液(W)の保有排熱をヒートポ
ンプ(35)により汲み上げて、その汲み上げ排熱を空
調用熱量の一部に再利用するようにしても良い。
Further, as shown in FIG. 4, a heat pump (35) is provided to heat the air conditioning heat medium used in the air conditioner (3), and
A container (2) forming a low pressure space in which the cleaning liquid (W) is evaporated.
8), the heat receiving side heat exchanger (31) of the heat pump (35) is installed inside the heat pump (35).
The vaporized cleaning liquid (W) is condensed through heat exchange between the working heat medium and the vaporized cleaning liquid (for example), and the waste heat retained in the cleaning liquid (W) is pumped up by the heat pump (35), and the pumped waste heat is used as the heat source for air conditioning. You may reuse some of them.

すなわち、気化洗浄液(−)と熱交換させる熱回収用熱
媒としては、空調器(3)で用いる空調用熱媒、空調器
(3)への取入外気、あるいは、空調用熱媒を加熱する
ヒートポンプ(35)の作動熱媒等、気体液体を問わず
種々のものを適用でき、又、気化洗浄液(−)から回収
した排熱を空調用途以外で利用するように熱回収用熱媒
を選定しても良い。
In other words, the heat recovery heat medium to be used for heat exchange with the vaporized cleaning liquid (-) may be an air conditioning heat medium used in the air conditioner (3), outside air taken into the air conditioner (3), or an air conditioning heat medium that heats the air conditioning heat medium. Various types of heating medium, whether gas or liquid, can be used as the operating heating medium for the heat pump (35), and a heating medium for heat recovery can be used so that the waste heat recovered from the vaporized cleaning liquid (-) can be used for purposes other than air conditioning. You may choose.

洗浄液(W)を蒸発させるための低圧空間を形成する気
化器の具体的構造は種々の改良が可能であり、又、真空
ポンプ(29)には、ターボ型や容積型、あるいは、エ
ゼクタ一方式によるものや化学作用を応用したもの等、
種々の型式のものを適用できる。
The specific structure of the vaporizer that forms a low-pressure space for evaporating the cleaning liquid (W) can be improved in various ways, and the vacuum pump (29) may be of a turbo type, a positive displacement type, or a single ejector type. and those that apply chemical effects, etc.
Various types can be applied.

気化洗浄液(W)と熱回収用熱媒とを熱交換させる熱交
換器(31)には種々の型式のものを適用できる。
Various types of heat exchangers (31) can be used for exchanging heat between the vaporized cleaning liquid (W) and the heat recovery heat medium.

気化器を構成する低圧空間形成用容器(28)の内周面
に対して高圧水や清浄洗浄水(匈)を吹付けるノズルを
設け、その吹付けにより容器(28)の内周面に対する
塗料の付着・堆積を防止するようにしても良い。
A nozzle is provided that sprays high-pressure water or clean washing water (xo) onto the inner circumferential surface of the container (28) for forming a low-pressure space that constitutes the vaporizer, and the spraying sprays paint onto the inner circumferential surface of the container (28). It may also be possible to prevent the adhesion and accumulation of.

又、気化洗浄液(W)中に極めて微細な塗料ミストが存
在し、その微細塗料ミストが熱交換器(31)に付着す
る虞れがある場合には、熱交換器(31)における気化
洗浄液(W)の凝縮部に対して高圧水や清浄洗浄液(W
)を適時、あるいは、間欠的に吹付けるノズルを設け、
それによって、熱交換器(31)に対する微細塗料ミス
トの付着・堆積をより一層確実に防止するようにしても
良い。
In addition, if extremely fine paint mist exists in the vaporized cleaning liquid (W) and there is a risk that the fine paint mist may adhere to the heat exchanger (31), the vaporized cleaning liquid (W) in the heat exchanger (31) may High pressure water or cleaning liquid (W) is applied to the condensation part of W).
) is installed at the right time or intermittently.
This may further reliably prevent fine paint mist from adhering to and accumulating on the heat exchanger (31).

気化器に供給する洗浄液(W)から予め塗料滓を分離除
去しておくフィルター等の各種塗料滓分離器(11)を
設けることは任意である。
It is optional to provide various types of paint sludge separators (11) such as filters for separating and removing paint sludge in advance from the cleaning liquid (W) supplied to the vaporizer.

洗浄液(−)としては水の他に種々の液体を適用できる
。又、洗浄液(W)にカセイソーダ等の各種塗料粘着性
低下薬を混入してお(ことは気化器への塗料付着を防止
する上で有効である。
As the cleaning liquid (-), various liquids other than water can be used. In addition, various paint tack reducing agents such as caustic soda are mixed into the cleaning liquid (W) (this is effective in preventing paint from adhering to the vaporizer).

空調器(3)から塗装作業域(2)へ供給する温調換気
気体は空気に限定されるものでは無い。
The temperature-controlled ventilation gas supplied from the air conditioner (3) to the painting work area (2) is not limited to air.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の第1実施例を示す構成図である。第2
図は本発明の第2実施例を示す構成図である。第3図及
び第4図は夫々その他の実施例を示す構成図である。第
5図及び第6図は夫々従来例を示す構成図である。 (2)・・・・・・塗装作業域、(3)・・・・・・空
調器、(8)・・・・・・塗料ミスト除去装置、(31
)・・・・・・熱交換器、(W)・・・・・・洗浄液。
FIG. 1 is a block diagram showing a first embodiment of the present invention. Second
The figure is a configuration diagram showing a second embodiment of the present invention. FIGS. 3 and 4 are configuration diagrams showing other embodiments, respectively. FIGS. 5 and 6 are configuration diagrams showing conventional examples, respectively. (2)...Painting work area, (3)...Air conditioner, (8)...Paint mist removal device, (31
)...Heat exchanger, (W)...Cleaning liquid.

Claims (3)

【特許請求の範囲】[Claims] (1)塗装作業域(2)への供給換気気体を温調する空
調器(3)、及び、前記塗装作業域(2)からの排気気
体と洗浄液(W)とを接触させて排気気体中の塗料ミス
トを捕捉除去する塗料ミスト除去装置(8)を備えた塗
装ブースであって、前記塗料ミスト除去装置(8)にお
いて洗浄作用した後の洗浄液(W)を蒸発させるための
低圧空間を形成する気化器を設け、その気化器において
蒸発した気化洗浄液(W)と熱回収用熱媒とを熱交換さ
せて気化洗浄液(W)から凝縮熱を奪うことにより前記
塗装作業域(2)からの排熱を回収する熱交換器(31
)を設けた塗装ブース。
(1) An air conditioner (3) that controls the temperature of the ventilation gas supplied to the painting work area (2), and an air conditioner (3) that controls the temperature of the ventilation gas supplied to the painting work area (2), and a cleaning liquid (W) that brings the exhaust gas from the painting work area (2) into contact with the exhaust gas. A painting booth is equipped with a paint mist removal device (8) that captures and removes paint mist, and forms a low-pressure space for evaporating the cleaning liquid (W) after the cleaning action in the paint mist removal device (8). A vaporizer is installed to remove the heat of condensation from the vaporized cleaning liquid (W) by exchanging heat between the vaporized cleaning liquid (W) and a heat recovery heat medium in the vaporizer, thereby removing the condensation heat from the painting work area (2). Heat exchanger to recover waste heat (31
) painting booth.
(2)前記熱回収用熱媒が前記空調器(3)で使用する
空調用熱媒液である特許請求の範囲第(1)項に記載の
塗装ブース。
(2) The painting booth according to claim (1), wherein the heat recovery heat medium is an air conditioning heat medium liquid used in the air conditioner (3).
(3)前記熱回収用熱媒が前記空調器(3)に対する取
入外気である特許請求の範囲第(1)項に記載の塗装ブ
ース。
(3) The painting booth according to claim (1), wherein the heat medium for heat recovery is outside air taken into the air conditioner (3).
JP61120757A 1986-05-26 1986-05-26 Painting booth Pending JPS62277174A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61120757A JPS62277174A (en) 1986-05-26 1986-05-26 Painting booth

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61120757A JPS62277174A (en) 1986-05-26 1986-05-26 Painting booth

Publications (1)

Publication Number Publication Date
JPS62277174A true JPS62277174A (en) 1987-12-02

Family

ID=14794236

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61120757A Pending JPS62277174A (en) 1986-05-26 1986-05-26 Painting booth

Country Status (1)

Country Link
JP (1) JPS62277174A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017119257A (en) * 2015-12-29 2017-07-06 金沢ロック株式会社 Coating booth for water paint

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5236333A (en) * 1975-09-17 1977-03-19 Showa Shell Sekiyu Kk Process to decrease generation of nitrogen oxide in exhaust gas
JPS61242663A (en) * 1985-04-20 1986-10-28 Toyota Motor Corp Process for recovering waste heat from painting booth

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5236333A (en) * 1975-09-17 1977-03-19 Showa Shell Sekiyu Kk Process to decrease generation of nitrogen oxide in exhaust gas
JPS61242663A (en) * 1985-04-20 1986-10-28 Toyota Motor Corp Process for recovering waste heat from painting booth

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017119257A (en) * 2015-12-29 2017-07-06 金沢ロック株式会社 Coating booth for water paint

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