JPH067635A - Organic solvent removing device for coating booth with dehumidifying and humidifying functions - Google Patents

Organic solvent removing device for coating booth with dehumidifying and humidifying functions

Info

Publication number
JPH067635A
JPH067635A JP4191618A JP19161892A JPH067635A JP H067635 A JPH067635 A JP H067635A JP 4191618 A JP4191618 A JP 4191618A JP 19161892 A JP19161892 A JP 19161892A JP H067635 A JPH067635 A JP H067635A
Authority
JP
Japan
Prior art keywords
organic solvent
dehumidifying
coating
heating
exhaust
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.)
Withdrawn
Application number
JP4191618A
Other languages
Japanese (ja)
Inventor
Takao Iwamoto
隆夫 岩本
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.)
HIROSHIMA GAS KAIHATSU KK
Original Assignee
HIROSHIMA GAS KAIHATSU KK
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 HIROSHIMA GAS KAIHATSU KK filed Critical HIROSHIMA GAS KAIHATSU KK
Priority to JP4191618A priority Critical patent/JPH067635A/en
Publication of JPH067635A publication Critical patent/JPH067635A/en
Withdrawn legal-status Critical Current

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Landscapes

  • Central Air Conditioning (AREA)
  • Treating Waste Gases (AREA)
  • Drying Of Gases (AREA)
  • Details Or Accessories Of Spraying Plant Or Apparatus (AREA)
  • Coating Apparatus (AREA)

Abstract

PURPOSE:To economically obtain the appropriate atmosphere for coating work in a coating booth by dehumidifying or humidifying the purified gas having been remove organic solvent from waste gas in the coating booth to obtain and returning it to the coating booth again. CONSTITUTION:To an exhaust pipe 11 connected to the exhaust port of a coating booth 1 in which coating is performed by using a coating material contg. organic solvent, a concentrating deodorizing device 13 for removing organic solvent in waste gas through an exhaust filter 12 is installed. On the downstream side of the concentrating/deodorizing device 13, a dehumidifying/humidifying device 5 for dehumidifying or humidifying the purified gas from which organic solvent has been separated is installed. The purified gas from the dehumidifying/ humidifying device is supplied to an intake pipe 10 connected to the intake port of the coating booth 1 through a fan 9.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、有機溶剤を含有する塗
料を塗装する塗装室から排出される排気ガス中の有機溶
剤の除去と該塗装室内を除湿又は加温する装置に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for removing an organic solvent in exhaust gas discharged from a coating chamber for coating a paint containing an organic solvent and for dehumidifying or heating the coating chamber.

【0002】[0002]

【従来の技術】有機溶剤を含有する塗料を用いて塗装す
る塗装室から排出される排気ガス中の有機溶剤を除去
し、かつ塗装作業に適切な塗装室内の温・湿度条件を保
つために、従来は図3に示す様に、塗装室1の排気側に
有機溶剤を除去する濃縮脱臭装置13を、又、塗装室1
の給気側に除湿及び加温の切り替え可能な除湿・加温装
置5を別個に設備している。
2. Description of the Related Art In order to remove the organic solvent contained in the exhaust gas discharged from a coating chamber for coating with a coating containing an organic solvent, and to maintain the temperature and humidity conditions in the coating chamber suitable for coating work, Conventionally, as shown in FIG. 3, a concentrated deodorizing device 13 for removing an organic solvent is provided on the exhaust side of the coating chamber 1, and also the coating chamber 1
A dehumidifying / warming device 5 capable of switching between dehumidifying and heating is separately provided on the air supply side.

【0003】つまり、塗装室1から排出される有機溶剤
を含んだ排気を排気管11により排気用フィルター12
に通じて塗料ミストを除去した後、濃縮脱臭装置13に
て排気中の有機溶剤を除去し、この浄化ガスを送気管1
4により排気ファン15を経て排気管16により大気中
に排出している。
That is, the exhaust gas containing the organic solvent discharged from the coating chamber 1 is exhausted through the exhaust pipe 11 to the exhaust filter 12
After removing the paint mist through the exhaust pipe, the concentrated deodorizing device 13 removes the organic solvent in the exhaust gas, and the purified gas is supplied to the air pipe 1
4 through the exhaust fan 15 and the exhaust pipe 16 into the atmosphere.

【0004】濃縮脱臭装置13では、再生用外気17を
再生加熱器18にて加熱して再生熱風19を作り、これ
を通過させて有機溶剤を分離させ、再生する。この再生
熱風19は有機溶剤を含んだ排気ガスより非常に小さい
風量であるので、濃縮脱臭装置13内にて濃縮された有
機溶剤を含んだ排気20は、再生ファン21を介し、有
機溶剤分解装置22にて、小さなエネルギーによって容
易に有機溶剤を除去することが可能であり、浄化された
浄化ガス23は外気へ排出される。
In the concentrating deodorizing device 13, the outside air 17 for regeneration is heated by a regeneration heater 18 to produce a regenerated hot air 19, which is passed to separate the organic solvent and regenerate. Since this regenerated hot air 19 has a much smaller air volume than the exhaust gas containing the organic solvent, the exhaust gas 20 containing the organic solvent concentrated in the concentration deodorizing device 13 is passed through the regeneration fan 21 to the organic solvent decomposing device. At 22, it is possible to easily remove the organic solvent with a small amount of energy, and the purified gas 23 thus purified is discharged to the outside air.

【0005】しかしながら、前記の装置において塗装室
1内の空気を排出するに当っては、塗装室1内へ外気を
導入する必要があり、この場合、塗装室内の温・湿度条
件を適切に保つために、導入する給気用外気2を給気用
フィルター3で除塵した後、送気管4を介して除湿及び
加温の切り替え可能な除湿・加温装置5を通過させて、
除湿が必要な時は該装置に冷水を通じて冷却除湿し、加
温が必要な時は該装置に温水を通じて加温し、その空気
を給気ファン9を経て給気管10により、塗装室1へ給
気している。
However, when the air in the coating chamber 1 is exhausted by the above-mentioned apparatus, it is necessary to introduce the outside air into the coating chamber 1. In this case, the temperature and humidity conditions in the coating chamber are appropriately maintained. In order to remove the dust from the introduced outside air 2 for air supply by the air supply filter 3, it is passed through the dehumidification / heating device 5 capable of switching between dehumidification and heating via the air supply pipe 4,
When dehumidification is required, cold water is passed through the device to cool and dehumidify it, and when warming is required, warm water is heated to the device and the air is supplied to the coating chamber 1 through the air supply fan 9 and the air supply pipe 10. I care.

【0006】除湿・加温装置5には、その冷・熱源とし
て冷・温水7が必要であるが、これは別途に設けた冷・
温水発生機6にて循環水を冷却もしくは加熱して、冷・
温水ポンプ8により循環使用している。なお、除湿装置
が冷却式である場合について説明したが、これは吸着剤
を用いた吸着式除湿装置の場合も同様である。
The dehumidifying / warming device 5 requires cold / hot water 7 as its cold / heat source, which is provided separately.
Cooling or heating the circulating water with the hot water generator 6
It is circulated and used by the hot water pump 8. The case where the dehumidifying device is of the cooling type has been described, but the same applies to the case of the adsorption type dehumidifying device using an adsorbent.

【0007】[0007]

【発明が解決しようとする課題】塗装室の排気風量は、
塗装室内部の有機溶剤濃度をなるべく低くすることが要
求されるため大風量となる。これに伴って給気風量も大
となるので除湿・加温装置についても容量の非常に大き
なものが必要となるため、現実には、排気ガス中の有機
溶剤の除去と塗装室内の温・湿度を適切にすることので
きる設備を設置することは不可能に近かった。
[Problems to be Solved by the Invention]
Since it is required to lower the concentration of the organic solvent in the coating chamber as much as possible, the air volume becomes large. Along with this, the supply air volume also becomes large, so a dehumidifying / heating device with a very large capacity is also required.In reality, the removal of the organic solvent in the exhaust gas and the temperature / humidity in the coating chamber are required. It was almost impossible to install equipment that could make

【0008】又、仮に大容量の装置を設置したとしても
塗装室内の雰囲気を一定の条件に保つには長時間を要
し、極めて不経済なものとならざるを得ないものであっ
た。そこで、効率よく排気ガス中の有機溶剤を除去し、
なおかつ、小容量の除湿・加温装置にて、塗装室内の空
気を除湿又は加温し塗装室内を塗装作業に適切な雰囲気
に保つことができる装置を提供することを本発明の課題
とするものである。
Further, even if a large-capacity device is installed, it takes a long time to maintain the atmosphere in the coating chamber under constant conditions, which is unavoidably uneconomical. Therefore, efficiently remove the organic solvent in the exhaust gas,
Further, it is an object of the present invention to provide a device capable of dehumidifying or heating the air in the coating chamber to maintain an atmosphere suitable for coating work in the coating chamber with a small capacity dehumidifying / heating device. Is.

【0009】[0009]

【課題を解決するための手段】本発明に係る除湿及び加
温機能付き塗装室用有機溶剤除去装置は、従来、塗装室
の排気側と給気側とにそれぞれ別個に設置されていた濃
縮脱臭装置13と、除湿・加温装置5又は冷却式除湿装
置24と加熱装置29とを一つの循環する配管系内に一
体の設備として配置することを、上記の課題を解決する
ための手段とするものである。
The organic solvent removing device for a coating chamber with dehumidifying and heating functions according to the present invention has been conventionally installed separately on the exhaust side and the air supplying side of the coating chamber. Arranging the device 13, the dehumidifying / warming device 5 or the cooling type dehumidifying device 24 and the heating device 29 as an integrated facility in one circulating piping system is a means for solving the above problems. It is a thing.

【0010】すなわち、本発明の第1は、有機溶剤を含
有する塗料を用いて塗装を行なう塗装室1の排気口に接
続される排気管11に、排気用フィルター12を介して
排気ガス中の有機溶剤を除去する濃縮脱臭装置13を設
け、該濃縮脱臭装置13の下流側に有機溶剤が除去され
た浄化ガスを除湿又は加温する除湿・加温装置5を設
け、該除湿・加温装置からの浄化ガスを、ファン9を介
して前記塗装室1の給気口に接続される給気管10に給
気するようにした塗装室用の除湿及び加温機能付き有機
溶剤除去装置であり、
That is, the first aspect of the present invention is that the exhaust pipe 11 connected to the exhaust port of the coating chamber 1 for performing the coating using the coating material containing the organic solvent is connected to the exhaust pipe 12 through the exhaust filter 12, The concentrated deodorizing device 13 for removing the organic solvent is provided, and the dehumidifying / heating device 5 for dehumidifying or heating the purified gas from which the organic solvent has been removed is provided on the downstream side of the concentrated deodorizing device 13. Is a dehumidifying and heating organic solvent removing device for a coating chamber, in which the purified gas from is supplied to the air supply pipe 10 connected to the air supply port of the coating chamber 1 through a fan 9.

【0011】本発明の第2は、有機溶剤を含有する塗料
を用いて塗装を行なう塗装室1の排気口に接続される排
気管11に排気用フィルター12を介して冷却式除湿装
置24を設けると共にその下流側に有機溶剤を除去する
濃縮脱臭装置13を設け、該濃縮脱臭装置の下流側に有
機溶剤が除去された浄化ガスを加温する加温装置29を
設け、該加温装置29からの浄化ガスを、ファン9を介
して前記塗装室1の給気口に接続される給気管10に給
気するようにした塗装室用の除湿及び加温機能付き有機
溶剤除去装置である。
A second aspect of the present invention is to provide a cooling type dehumidifying device 24 via an exhaust filter 12 in an exhaust pipe 11 connected to an exhaust port of a coating chamber 1 for coating with a coating material containing an organic solvent. At the same time, a concentration deodorizing device 13 for removing the organic solvent is provided on the downstream side thereof, and a heating device 29 for heating the purified gas from which the organic solvent has been removed is provided on the downstream side of the concentration deodorizing device. Is an organic solvent removing device with a dehumidifying and heating function for a coating chamber, in which the purified gas is supplied to a gas supply pipe 10 connected to a gas supply port of the coating chamber 1 via a fan 9.

【0012】[0012]

【作用】濃縮脱臭装置にて排気ガス中の有機溶剤を除去
された浄化ガスと云えども有機溶剤は皆無ではないが、
適切な運転条件下では、数PPMの濃度であり、その浄
化ガスを再び塗装室へ給気しても十分な排気風量さえあ
れば、塗装室内は、作業員に対しても何ら問題のない有
機溶剤濃度の雰囲気となるため継続的な塗装作業が可能
となる。
[Function] Even though it is a purified gas in which the organic solvent in the exhaust gas has been removed by the concentration deodorizing device, there is no organic solvent at all,
Under appropriate operating conditions, the concentration is several PPM, and even if the purified gas is supplied to the coating room again, as long as the exhaust air volume is sufficient, the inside of the coating room will not cause any problems for workers. Since the atmosphere has a solvent concentration, continuous painting work is possible.

【0013】しかも、濃縮脱臭装置では、湿分は減少
し、減少しなくとも加湿されることは無い為、除湿され
た浄化ガスを再び塗装室内に給気できることになる。
又、温度条件的には濃縮脱臭装置での排気ガスの昇温は
ごくわずかであるため、冷却除湿装置の負荷にはあまり
影響を与えず、逆に、加熱時には加温装置の負荷を減ず
る効果がある。
Moreover, in the concentration deodorizing device, the moisture content is reduced and is not humidified even if it is not reduced, so that the dehumidified purified gas can be supplied to the coating chamber again.
Also, in terms of temperature conditions, the temperature rise of exhaust gas in the concentration deodorizing device is very small, so it does not affect the load of the cooling and dehumidifying device so much, and conversely, the effect of reducing the load of the heating device during heating. There is.

【0014】[0014]

【実施例】以下、図によって本発明の実施例を説明す
る。図1は、本発明の第1の実施例を示すものであり、
図2は、本発明の第2の実施例を示すものである。な
お、各図において、従来例を示す図3と同様のものは同
一符号を付し説明を省略する。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows a first embodiment of the present invention,
FIG. 2 shows a second embodiment of the present invention. In each drawing, the same parts as those in FIG. 3 showing the conventional example are designated by the same reference numerals and the description thereof will be omitted.

【0015】まず、第1実施例は図1に示すように、有
機溶剤を含有する塗料を用いて塗装を行なう塗装室1の
排気口に接続される排気管11に、排気用フィルター1
2を介して排気ガス中の有機溶剤を除去する濃縮脱臭装
置13を設け、該濃縮脱臭装置13の下流側に有機溶剤
が除去された浄化ガスを除湿又は加温する除湿・加温装
置5を設け、該除湿・加温装置からの浄化ガスを、ファ
ン9を介して前記塗装室1の給気口に接続される給気管
10に給気するようにした塗装室用の除湿及び加温機能
付き有機溶剤除去装置である。
First, in the first embodiment, as shown in FIG. 1, an exhaust filter 1 is attached to an exhaust pipe 11 connected to an exhaust port of a coating chamber 1 for coating with a paint containing an organic solvent.
2 is provided with a concentration deodorizing device 13 for removing the organic solvent in the exhaust gas, and a dehumidifying / heating device 5 for dehumidifying or heating the purified gas from which the organic solvent has been removed is provided on the downstream side of the concentration deodorizing device 13. A dehumidifying and heating function for a coating chamber, which is provided and supplies purified gas from the dehumidifying / warming device to a gas supply pipe 10 connected to a gas supply port of the coating chamber 1 through a fan 9. It is a device for removing organic solvent.

【0016】上記の第1の実施例では、濃縮脱臭装置1
3にて有機溶剤を除去して、浄化された浄化ガスを屋外
へ排出せず、送気管14にて導き、除湿・加温装置5を
通過させて、除湿が必要な時は該装置に冷水を通じて冷
却除湿し、加温が必要な時は該装置に温水を通じて加温
し、その空気を給気ファン9を経て給気管10により塗
装室1へ給気している。
In the first embodiment, the concentration deodorizing device 1 is used.
In step 3, the organic solvent is removed, and the purified gas that has been purified is not discharged to the outdoors, but is guided by the air supply pipe 14 and passed through the dehumidifying / warming device 5. When dehumidifying is necessary, cold water is supplied to the device. When the heating is required, the apparatus is heated with hot water, and the air is supplied to the coating chamber 1 through the air supply fan 9 and the air supply pipe 10.

【0017】今、第一実施例の装置を、橋梁鉄骨塗装室
に設置して稼働させた具体例を、比較例とともに述べれ
ば、次の通りである。なお、上記塗装室の主要な条件は
以下の通りである。
Now, a concrete example in which the apparatus of the first embodiment is installed and operated in a bridge steel frame coating room will be described below together with a comparative example. The main conditions of the coating room are as follows.

【0018】上記塗装室に、図3に示した従来技術の装
置を設置して稼働させた場合と、第1実施例である図1
に示す装置を設置して稼働させた場合とを比較する。濃
縮脱臭装置13等の排気処理設備は両装置とも同容量と
なるが、除湿・加温装置5の容量は、従来技術の装置
と、第一実施例の装置では必要設備容量が大巾に異なっ
たものとなる。即ち、除湿・加温装置の容量を比較して
みると、塗装室の熱負荷や水分負荷は両装置とも同じで
あるが、従来技術の装置では、濃縮脱臭装置13の排気
700Nm3 /MIN全てを排出するために、この排気と同量の
700Nm3 /MINの外気を除湿・加温装置にて除湿又は加温
して給気しなければならないことになる。これに対し、
第一実施例の装置の場合には濃縮脱臭装置13から排出
された浄化ガスを除湿又は加温すれば良いから、外気負
荷に相当する負荷が大巾に減じられることになる。
The case where the apparatus of the prior art shown in FIG. 3 is installed and operated in the coating chamber and the case of the first embodiment shown in FIG.
Compare with the case where the device shown in (1) is installed and operated. Exhaust treatment equipment such as the concentration deodorizing device 13 has the same capacity in both devices, but the capacity of the dehumidifying / warming device 5 is significantly different from the conventional device and the device of the first embodiment. It becomes a thing. That is, comparing the capacities of the dehumidifying / heating devices, the heat load and the water load of the coating chamber are the same in both devices, but in the device of the prior art, the exhaust gas of the concentration deodorizing device 13 is exhausted.
In order to discharge all 700Nm 3 / MIN, the same amount as this exhaust
The outside air of 700 Nm 3 / MIN must be dehumidified or heated by the dehumidifying / heating device to supply air. In contrast,
In the case of the device of the first embodiment, the purified gas discharged from the concentration deodorizing device 13 may be dehumidified or heated, so that the load corresponding to the outside air load can be greatly reduced.

【0019】除湿運転時にあっては、従来技術の装置で
は、外気の持つエンタルピーは、iOA1 =23.0kcal/kg'
で、塗装室内の空気の持つエンタルピーは、ip=20.4Kc
al/kg'であるので、その外気負荷は、 q1 =( 23.0−2
0.4 )×1.29× 700×60=140,868kcal/HRとなるが、第
一実施例の装置では塗装室からの排気は、濃縮脱臭装置
にて約1℃温度が上昇するのみで、水分値は同一か、も
しくは絶対湿度にて 1g/Nm3 程度減少する。
At the time of dehumidification operation, the enthalpy of the outside air is i OA1 = 23.0 kcal / kg 'in the conventional device.
So, the enthalpy of the air in the painting room is ip = 20.4Kc
al / kg ', the external air load is q 1 = (23.0−2
0.4) × 1.29 × 700 × 60 = 140,868 kcal / HR, but in the device of the first embodiment, the temperature of the exhaust gas from the coating chamber rises only about 1 ° C. in the deodorizing device, and the water content is the same. Or, it decreases by about 1g / Nm 3 in absolute humidity.

【0020】今設備に余裕を持たせるために悪い方の条
件、即ち、温度は1℃上昇、水分値は同一の方を計算条
件として採用しても、除湿・加温コイル5への入口エン
タルピーは、i OA2 =20.6kcal/kg'( 31℃、21.6g/kg')
となり、その外気負荷は q2=(20.6 −20.4) ×1.29×7
00 ×60=10,836kcal/HR となるから、従来技術の装置
の1/10以下の外気負荷になる。
Even if the worse condition is used to make room for the equipment, that is, the temperature rises by 1 ° C. and the moisture content is the same as the calculation condition, the enthalpy at the entrance to the dehumidifying / heating coil 5 is increased. Is i OA2 = 20.6kcal / kg '(31 ℃, 21.6g / kg')
And the outside air load is q 2 = (20.6 −20.4) × 1.29 × 7
Since 00 × 60 = 10,836 kcal / HR, the external air load is 1/10 or less that of the conventional device.

【0021】加温運転時にあっては、同様に従来技術の
装置の外気負荷は、 q3 =0.31×10×700 ×60=130,20
0kcal/HRとなるが、第一実施例の装置では前述の様に、
逆に濃縮脱臭装置にて約1℃温度が上昇するため負荷で
なく給熱となるが、設備に余裕を持たせるためにその1
℃の温度上昇は無視したとしても、約130,000kcal/HRの
容量減少が図れる。
During the heating operation, the outside air load of the prior art device is also q 3 = 0.31 × 10 × 700 × 60 = 130,20
Although it becomes 0 kcal / HR, in the device of the first embodiment, as described above,
On the other hand, the temperature rises by about 1 ° C in the concentrating deodorizer, so heat is supplied instead of a load.
Even if the temperature rise of ℃ is ignored, the capacity can be reduced by about 130,000 kcal / HR.

【0022】なお、上記においては、除湿装置を冷却式
で説明したが、吸着剤を用いた吸着式除湿装置でも、効
果は同様となる。
In the above description, the dehumidifying device is described as a cooling type, but the same effect can be obtained with an adsorption type dehumidifying device using an adsorbent.

【0023】次に、図2にて、本発明の第2の実施例に
ついて説明する。 第2実施例は図2に示すように、有
機溶剤を含有する塗料を用いて塗装を行なう塗装室1の
排気口に接続される排気管11に排気用フィルター12
を介して冷却式除湿装置24を設けると共にその下流側
に有機溶剤を除去する濃縮脱臭装置13を設け、該濃縮
脱臭装置の下流側に有機溶剤が除去された浄化ガスを加
温する加温装置29を設け、該加温装置29からの浄化
ガスを、ファン9を介して前記塗装室1の給気口に接続
される給気管10に給気するようにした塗装室用の除湿
及び加温機能付き有機溶剤除去装置である。
Next, a second embodiment of the present invention will be described with reference to FIG. In the second embodiment, as shown in FIG. 2, an exhaust filter 12 is attached to an exhaust pipe 11 connected to an exhaust port of a coating chamber 1 in which a coating material containing an organic solvent is used for coating.
A cooling type dehumidifying device 24 is provided through the same, a concentration deodorizing device 13 for removing an organic solvent is provided on the downstream side thereof, and a heating device for heating the purified gas from which the organic solvent has been removed is provided on the downstream side of the concentration deodorizing device. Dehumidification and heating for a coating chamber in which the purified gas from the heating device 29 is provided to the air supply pipe 10 connected to the air supply port of the coating chamber 1 through the fan 9. It is an organic solvent removal device with a function.

【0024】上記の第2実施例では、除湿手段を冷却方
式とした場合に、より効率よく除湿が可能で、かつ、脱
臭効率をあげることができ、排気用フィルター12にて
塗料ミストを除去した後、まず冷却式除湿装置24に通
じて、冷却除湿した排気を送気管28により濃縮脱臭装
置13に送り込むことにより、低温状態にして吸着効率
を上昇させる効果が得られるとともに、濃縮脱臭装置1
3での水分吸着効果も上昇させることが出来、除湿効果
も向上させることができる。
In the above second embodiment, when the dehumidifying means is a cooling system, dehumidification can be performed more efficiently and deodorizing efficiency can be improved, and the paint mist is removed by the exhaust filter 12. After that, first, the exhaust gas that has been cooled and dehumidified is first sent to the cooling type dehumidifying device 24 and sent to the concentrating deodorizing device 13 through the air supply pipe 28, so that an effect of increasing the adsorption efficiency can be obtained in a low temperature state, and at the same time, the concentrating deodorizing device 1 can be obtained.
The water adsorption effect in 3 can be increased, and the dehumidification effect can be improved.

【0025】これは、通常用いられる濃縮脱臭装置は、
活性炭かゼオライトが用いられており、処理空気温度の
低い方が、有機溶剤及び水分の吸着効果が上昇するから
である。この場合、加温の必要な場合は、排出された浄
化ガスを送気管14により加温装置29に通じて加温
し、給気ファン9を介し給気管10により塗装室1へ給
気する。
This is because a commonly used concentration deodorizing device is
This is because activated carbon or zeolite is used, and the lower the treatment air temperature, the higher the adsorption effect of the organic solvent and water. In this case, when heating is necessary, the discharged purified gas is supplied to the heating device 29 by the air supply pipe 14 to be heated, and is supplied to the coating chamber 1 by the air supply pipe 10 via the air supply fan 9.

【0026】前記、冷却式除湿装置24の冷却源は、冷
水発生機25にて、冷水26を冷却し、冷水ポンプ27
にて循環して使用する。又、加温装置29の加温源は、
温水発生機30にて、温水31を加熱し、温水ポンプ3
2にて循環して使用する。なお、この温水発生手段は、
本実施例以外に電気や蒸気又は燃焼排ガスの熱交換にて
行うことも可能であるし、冷温水を発生させるヒートポ
ンプ式冷温水機を使用することも可能である。
As the cooling source of the cooling type dehumidifying device 24, the cold water generator 25 cools the cold water 26 and the cold water pump 27 is used.
Circulate and use. The heating source of the heating device 29 is
The hot water 31 is heated by the hot water generator 30, and the hot water pump 3
Circulate at 2 and use. In addition, this hot water generating means,
Other than this embodiment, it is also possible to perform heat exchange of electricity, steam or combustion exhaust gas, and it is also possible to use a heat pump type chiller / heater that generates chilled / hot water.

【0027】[0027]

【発明の効果】以上の如く、本発明の除湿及び加温機能
付き塗装室用有機溶剤除去装置によれば、除湿及び加温
装置の設備容量を大巾に減少できるので、設備費及び運
転費のコストダウンがはかれる。即ち、塗装室の除湿・
加温に用いられている従来技術の装置では、通常その7
5%程度が外気負荷であったから、本発明の装置では、
除湿装置でその除湿容量が70%程度、加温容量で75
%程度の容量を従来技術の装置より減少させることが可
能である。
As described above, according to the organic solvent removing apparatus for a coating chamber with the dehumidifying and heating function of the present invention, the equipment capacity of the dehumidifying and heating apparatus can be greatly reduced. The cost can be reduced. That is, dehumidification of the coating room
Prior art devices used for warming typically have
Since about 5% was the outside air load, in the device of the present invention,
The dehumidifier has a dehumidifying capacity of about 70% and a heating capacity of 75%.
It is possible to reduce the capacity in the order of% over prior art devices.

【0028】また、効率よく経済的に塗装室内の雰囲気
を所定の条件にすることができるので塗装の品質の向上
及び塗装工程管理の安定に貢献することができる。
Further, since the atmosphere in the coating chamber can be efficiently and economically set to a predetermined condition, the quality of coating can be improved and the control of the coating process can be stabilized.

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

【図1】本発明に係る第1実施例の回路図。FIG. 1 is a circuit diagram of a first embodiment according to the present invention.

【図2】本発明に係る第2実施例の回路図。FIG. 2 is a circuit diagram of a second embodiment according to the present invention.

【図3】従来技術による実施例の回路図。FIG. 3 is a circuit diagram of an embodiment according to the related art.

【符号の説明】[Explanation of symbols]

1 塗装室 5 除湿・加温装置 6 冷・温水発生機 8 冷・温水ポンプ 9 給気ファン 12 排気用フィルター 13 濃縮脱臭装置 18 再生加熱器 21 再生ファン 22 有機溶剤分解装置 24 冷却式除湿装置 25 冷水発生機 27 冷水ポンプ 29 加温装置 30 温水発生機 32 温水ポンプ 1 Painting Room 5 Dehumidification / Warming Device 6 Cold / Hot Water Generator 8 Cold / Hot Water Pump 9 Air Supply Fan 12 Exhaust Filter 13 Concentration Deodorizer 18 Regeneration Heater 21 Regeneration Fan 22 Organic Solvent Decomposition Device 24 Cooling Dehumidification Device 25 Cold water generator 27 Cold water pump 29 Heating device 30 Hot water generator 32 Hot water pump

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 F24F 3/16 6803−3L ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Internal reference number FI technical display location F24F 3/16 6803-3L

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 有機溶剤を含有する塗料を用いて塗装を
行なう塗装室1の排気口に接続される排気管11に、排
気用フィルター12を介して排気ガス中の有機溶剤を除
去する濃縮脱臭装置13を設け、該濃縮脱臭装置13の
下流側に有機溶剤が除去された浄化ガスを除湿又は加温
する除湿・加温装置5を設け、該除湿・加温装置からの
浄化ガスを、ファン9を介して前記塗装室1の給気口に
接続される給気管10に給気するようにした塗装室用の
除湿及び加温機能付き有機溶剤除去装置。
1. Concentrated deodorization for removing an organic solvent in exhaust gas through an exhaust filter 12 to an exhaust pipe 11 connected to an exhaust port of a coating chamber 1 for applying a coating containing an organic solvent. A device 13 is provided, and a dehumidifying / warming device 5 for dehumidifying or heating the purified gas from which the organic solvent has been removed is provided on the downstream side of the concentration / deodorization device 13, and the purified gas from the dehumidifying / heating device is blown by a fan. A dehumidifying and heating organic solvent removing device for a coating chamber, which supplies air to a gas supply pipe 10 connected to an air supply port of the coating chamber 1 via 9.
【請求項2】 有機溶剤を含有する塗料を用いて塗装を
行なう塗装室1の排気口に接続される排気管11に排気
用フィルター12を介して冷却式除湿装置24を設ける
と共にその下流側に有機溶剤を除去する濃縮脱臭装置1
3を設け、該濃縮脱臭装置の下流側に有機溶剤が除去さ
れた浄化ガスを加温する加温装置29を設け、該加温装
置29からの浄化ガスを、ファン9を介して前記塗装室
1の給気口に接続される給気管10に給気するようにし
た塗装室用の除湿及び加温機能付き有機溶剤除去装置。
2. A cooling type dehumidifying device 24 is provided through an exhaust filter 12 in an exhaust pipe 11 connected to an exhaust port of a coating chamber 1 for performing coating using a paint containing an organic solvent, and is provided on the downstream side thereof. Concentrating deodorizer 1 for removing organic solvent
3 is provided, a heating device 29 for heating the purified gas from which the organic solvent has been removed is provided on the downstream side of the concentration deodorizing device, and the purified gas from the heating device 29 is supplied to the coating chamber via the fan 9. An organic solvent removing device with a dehumidifying and heating function for a coating room, which is configured to supply air to an air supply pipe 10 connected to a first air supply port.
JP4191618A 1992-06-24 1992-06-24 Organic solvent removing device for coating booth with dehumidifying and humidifying functions Withdrawn JPH067635A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4191618A JPH067635A (en) 1992-06-24 1992-06-24 Organic solvent removing device for coating booth with dehumidifying and humidifying functions

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4191618A JPH067635A (en) 1992-06-24 1992-06-24 Organic solvent removing device for coating booth with dehumidifying and humidifying functions

Publications (1)

Publication Number Publication Date
JPH067635A true JPH067635A (en) 1994-01-18

Family

ID=16277635

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4191618A Withdrawn JPH067635A (en) 1992-06-24 1992-06-24 Organic solvent removing device for coating booth with dehumidifying and humidifying functions

Country Status (1)

Country Link
JP (1) JPH067635A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996030127A1 (en) * 1995-03-28 1996-10-03 Buchholz Leroy H Jr Closed system for volatile organic compound recycling
EP0798051A1 (en) * 1996-03-29 1997-10-01 Optimum Air Corporation Automated air filtration and drying system for waterborne paint and industrial coatings
WO1999031449A1 (en) * 1997-12-17 1999-06-24 Keld Gabelgaard Lacquer processing device and method
US5921002A (en) * 1993-09-24 1999-07-13 Optimum Air Corporation Radiation curing system
US6170427B1 (en) 1997-01-15 2001-01-09 Optimum Air Corporation Radiation curing system
JP2002186821A (en) * 2000-12-19 2002-07-02 Seibu Giken Co Ltd Organic solvent vapor treatment apparatus
JP2003007105A (en) * 2001-06-21 2003-01-10 Stanley Electric Co Ltd Manufacturing method of vehicle-use lens with moisture- proof coat film
JP2006015279A (en) * 2004-07-02 2006-01-19 Think Laboratory Co Ltd Coater for forming photosensitive film and plate making factory
JP2006292225A (en) * 2005-04-08 2006-10-26 Daikin Ind Ltd Refrigerating/air conditioning system
JP2007268643A (en) * 2006-03-31 2007-10-18 Jfe Mechanical Co Ltd Dehumidifying and dust removing system for blast chamber
JP2007268393A (en) * 2006-03-31 2007-10-18 Jfe Mechanical Co Ltd Dehumidification for paint chambers, and organic solvent treatment system
JP2010119901A (en) * 2008-11-17 2010-06-03 Trinity Ind Corp Exhaust recycle air conditioning system for coating booth
JP2010121783A (en) * 2008-11-17 2010-06-03 Trinity Ind Corp Exhaust dehumidification recycling air conditioning system of paint booth
JP2011088052A (en) * 2009-10-21 2011-05-06 Taikisha Ltd Coating apparatus
JP2012179602A (en) * 2012-05-24 2012-09-20 Jfe Mechanical Co Ltd Dehumidification and organic solvent treatment system for coating chamber
JP2018001045A (en) * 2016-06-27 2018-01-11 株式会社Japan Zero Painting system

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5921002A (en) * 1993-09-24 1999-07-13 Optimum Air Corporation Radiation curing system
US5970625A (en) * 1993-09-24 1999-10-26 Optimum Air Corporation Automated air filtration and drying system for waterborne paint and industrial coatings
WO1996030127A1 (en) * 1995-03-28 1996-10-03 Buchholz Leroy H Jr Closed system for volatile organic compound recycling
EP0798051A1 (en) * 1996-03-29 1997-10-01 Optimum Air Corporation Automated air filtration and drying system for waterborne paint and industrial coatings
EP0835694A1 (en) * 1996-03-29 1998-04-15 Optimum Air Corporation Method and apparatus for drying a product coated with a waterborne coating
US6170427B1 (en) 1997-01-15 2001-01-09 Optimum Air Corporation Radiation curing system
WO1999031449A1 (en) * 1997-12-17 1999-06-24 Keld Gabelgaard Lacquer processing device and method
JP2002186821A (en) * 2000-12-19 2002-07-02 Seibu Giken Co Ltd Organic solvent vapor treatment apparatus
JP4523146B2 (en) * 2000-12-19 2010-08-11 株式会社西部技研 Organic solvent vapor processing equipment
JP2003007105A (en) * 2001-06-21 2003-01-10 Stanley Electric Co Ltd Manufacturing method of vehicle-use lens with moisture- proof coat film
JP4522766B2 (en) * 2004-07-02 2010-08-11 株式会社シンク・ラボラトリー Photosensitive film coating apparatus and plate making factory
JP2006015279A (en) * 2004-07-02 2006-01-19 Think Laboratory Co Ltd Coater for forming photosensitive film and plate making factory
JP2006292225A (en) * 2005-04-08 2006-10-26 Daikin Ind Ltd Refrigerating/air conditioning system
JP2007268643A (en) * 2006-03-31 2007-10-18 Jfe Mechanical Co Ltd Dehumidifying and dust removing system for blast chamber
JP2007268393A (en) * 2006-03-31 2007-10-18 Jfe Mechanical Co Ltd Dehumidification for paint chambers, and organic solvent treatment system
JP2010119901A (en) * 2008-11-17 2010-06-03 Trinity Ind Corp Exhaust recycle air conditioning system for coating booth
JP2010121783A (en) * 2008-11-17 2010-06-03 Trinity Ind Corp Exhaust dehumidification recycling air conditioning system of paint booth
JP2011088052A (en) * 2009-10-21 2011-05-06 Taikisha Ltd Coating apparatus
JP2012179602A (en) * 2012-05-24 2012-09-20 Jfe Mechanical Co Ltd Dehumidification and organic solvent treatment system for coating chamber
JP2018001045A (en) * 2016-06-27 2018-01-11 株式会社Japan Zero Painting system

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