JPH11248347A - Drying furnace - Google Patents

Drying furnace

Info

Publication number
JPH11248347A
JPH11248347A JP4477398A JP4477398A JPH11248347A JP H11248347 A JPH11248347 A JP H11248347A JP 4477398 A JP4477398 A JP 4477398A JP 4477398 A JP4477398 A JP 4477398A JP H11248347 A JPH11248347 A JP H11248347A
Authority
JP
Japan
Prior art keywords
furnace
drying
furnace body
duct
gum
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.)
Granted
Application number
JP4477398A
Other languages
Japanese (ja)
Other versions
JP3655461B2 (en
Inventor
Mikio Murachi
知 幹 夫 村
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.)
Trinity Industrial Corp
Original Assignee
Trinity Industrial Corp
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 Trinity Industrial Corp filed Critical Trinity Industrial Corp
Priority to JP04477398A priority Critical patent/JP3655461B2/en
Publication of JPH11248347A publication Critical patent/JPH11248347A/en
Application granted granted Critical
Publication of JP3655461B2 publication Critical patent/JP3655461B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To reduce the labor required for cleaning the inside of a drying furnace, such as the drying furnace for painting, drying furnace for printing, etc., and, at the same time, to reduce the burden of an exhaust gas treating device. SOLUTION: A water electrolysis accelerating material 16 prepared by kneading the powder of a pyroelectric material with a heat-resistant organic adhesive is applied to the exposed internal surface 14 of the furnace casing 2, such as the furnace wall, etc., of a drying furnace. When the material 16 is heated as the temperature in the furnace rises, minus electric charges appear on the exposed internal surface 14 of the furnace casing 2 due to the pyroelectric effect of the material 16. When an evaporated organic solvent which is produced at the time of drying the coating film is condensed on the exposed internal surface 14 of the furnace casing 2, etc., and the condensed solvent adheres to the surface 14, etc., as gum, part of water molecules contained in the gum receives the electrons which appear due to the pyroelectric effect of the material 16 and electrolyzed into hydrogen and ionized oxygen. Since the ionized oxygen reacts to the organic matter which is the main component of the gum and dissolves the organic matter into water and carbon dioxide through oxidation, the quantity of the gum can be reduced.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、自動車ボディなど
の被塗物に塗布された塗料を乾燥したり、紙やプラスチ
ックなどに印刷された印刷インクを乾燥するために用い
られる乾燥炉に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a drying furnace used for drying a paint applied to an object to be coated such as an automobile body, and for drying a printing ink printed on paper or plastic.

【0002】[0002]

【従来の技術】例えば、自動車ボディの塗装ラインで
は、塗料を吹き付ける塗装ブースの後段に、その塗膜を
乾燥させる乾燥炉が設けられており、塗装終了直後の塗
膜が未乾燥の自動車ボディをコンベアで搬送しながら、
その表面に形成された塗膜を乾燥するようにしている。
乾燥炉は100〜160℃程度の温度に維持され、塗料
に含まれる水分や有機溶剤を蒸発させて塗膜を乾燥硬化
させているので、炉体内では有機溶剤濃度が徐々に高く
なっていき、これを放置すると、汚染空気に含まれる有
機溶剤が自動車ボディなどの被塗物表面に凝集して塗料
本来の色が褪せてしまい、黄変と称する塗装不良を生ず
ることとなる。このため、一般の乾燥炉では常に炉体内
から汚染空気(排ガス)を排出し、これを、排ガス処理
装置で浄化した後、炉体内に循環供給したり、あるい
は、大気に放出するようにしている。
2. Description of the Related Art For example, in a car body coating line, a drying oven for drying a coating film is provided at a stage subsequent to a coating booth for spraying a coating material. While transporting on a conveyor,
The coating film formed on the surface is dried.
Since the drying furnace is maintained at a temperature of about 100 to 160 ° C. and evaporates the moisture and organic solvent contained in the paint to dry and harden the coating film, the concentration of the organic solvent in the furnace gradually increases, If left untreated, the organic solvent contained in the contaminated air will agglomerate on the surface of the object to be coated such as an automobile body, causing the original color of the coating to fade, resulting in a coating defect called yellowing. For this reason, in a general drying furnace, contaminated air (exhaust gas) is always discharged from the inside of the furnace, and after being purified by an exhaust gas treatment device, the contaminated air (exhaust gas) is circulated and supplied into the furnace or discharged to the atmosphere. .

【0003】[0003]

【発明が解決しようとする課題】しかしながら、汚染空
気は外部へ排出されるまでの間に炉体内を対流するた
め、その汚染空気に含まれる蒸発有機溶剤が、側壁,天
井壁,床壁,仕切壁などの炉体内の表出面上に凝集し、
ヤニとなって付着するという問題があった。特に、天井
壁に付着したヤニが成長すると、被塗物の上にボタオチ
して塗装不良となるため、これを防止するためには、通
常でも2〜3週間ごとに、使用する塗料の種類によって
は毎週、炉体内を清掃しなければならない。しかも、自
動車ボディの塗装用乾燥炉は全長が百数十メートルもあ
り、その清掃作業は人手に頼らざるを得ないので多大な
労力を必要とし、清掃作業に要するコストが嵩むという
問題があった。
However, since the contaminated air convects inside the furnace before being discharged to the outside, the evaporated organic solvent contained in the contaminated air is removed from the side wall, the ceiling wall, the floor wall, and the partition. Agglomerates on exposed surfaces in the furnace, such as walls,
There was a problem that it adhered as a stain. In particular, if the tar attached to the ceiling wall grows, it will splatter on the object to be coated, resulting in poor coating. To prevent this, usually every two to three weeks, depending on the type of paint used, Must clean the inside of the furnace every week. In addition, the drying oven for painting the body of an automobile has a total length of more than one hundred and several hundred meters, and the cleaning operation has to rely on manual labor, so that a great deal of labor is required, and the cost required for the cleaning operation is increased. .

【0004】 また、塗装用乾燥炉は全長が長いことか
らその容積も大きく、排ガス処理装置では、この乾燥炉
から連続的に排出される大量の排ガスを浄化処理しなけ
ればならないことから、消費エネルギーが多く、消耗品
の交換や、排ガス処理装置に至るダクト内の清掃作業な
どに要するメンテナンスコスト及びランニングコストが
嵩むという問題があった。また、印刷用乾燥炉において
は、塗装用乾燥炉ほどではないが、印刷インクから有機
溶剤成分が蒸発する点では塗装用乾燥炉と共通し、その
蒸発有機溶剤による問題点も規模の違いこそあれ同様で
ある。
Further, the drying furnace for coating has a large volume due to its long overall length, and the exhaust gas treatment device has to purify a large amount of exhaust gas continuously discharged from the drying furnace. However, there is a problem that maintenance costs and running costs required for exchanging consumables and cleaning the inside of the duct leading to the exhaust gas treatment device are increased. Although the drying oven for printing is not as good as the drying oven for coating, the organic solvent component evaporates from the printing ink in common with the drying oven for coating. The same is true.

【0005】 そこで本発明は、塗装用乾燥炉や印刷用
乾燥炉などの乾燥炉内の清掃作業に要する労力を軽減す
ると共に、排ガス処理装置の負荷を軽減して、メンテナ
ンスコスト及びランニングコストを著しく低減すること
を技術的課題としている。
Accordingly, the present invention reduces the labor required for cleaning operations in a drying oven such as a coating drying oven or a printing drying oven, and reduces the load on an exhaust gas treatment apparatus, thereby significantly reducing maintenance costs and running costs. Reduction is a technical issue.

【0006】[0006]

【課題を解決するための手段】この課題を解決するため
に、本発明は、炉体内でワークを乾燥することにより蒸
発有機溶剤を含む汚染空気が生成される乾燥炉におい
て、炉体内の表出面、もしくは、炉体内の空気が流通す
るダクトの内面に、焦電材料の粉末を耐熱性の無機接着
剤に混練した水電解促進材が塗工されていることを特徴
とする。
SUMMARY OF THE INVENTION To solve this problem, the present invention relates to a drying furnace in which contaminated air containing an evaporated organic solvent is generated by drying a work in the furnace, and a surface of the furnace inside the furnace is provided. Alternatively, a water electrolysis accelerating material obtained by kneading a pyroelectric material powder with a heat-resistant inorganic adhesive is coated on an inner surface of a duct through which air in the furnace flows.

【0007】 本発明による乾燥炉は、例えば、有機溶
剤を含む塗料で塗装された自動車ボディを炉体内に搬入
して加熱すると塗膜が乾燥硬化していく。このとき、炉
体内の表出面や、炉体内の空気が流通するダクトの内面
には、焦電材料の粉末を耐熱性の無機接着剤に混練した
水電解促進材が塗工されているので、焦電材料が加熱さ
れたときに、その焦電効果により、炉体内の表出面やダ
クトの内面にマイナスの電荷が表れる。一方、ワークを
加熱すると、未乾燥塗膜から水分や有機溶剤が蒸発し、
これが炉体内の空気の対流に伴って、その表出面やダク
トの内面に付着凝集してヤニとなる。そして、このヤニ
の中に含まれる水の分子は、焦電効果により表れる電子
を受け取って、その一部は、 H2 O +2e- → O2- + H2 2 O + e- → O- + H2 で表される反応により、水素とイオン化された酸素に電
気分解される。そして、このイオン化された酸素が、炉
体内の表出面に付着しているヤニの主成分である有機物
と反応し、これを酸化して水と二酸化炭素に分解する。
したがって、炉体内の表出面に付着したヤニが徐々に分
解されて減量されていくので、その分、清掃作業の頻度
及び労力が軽減されると共に、排ガス処理装置の負荷も
軽減されて、メンテナンスコスト,ランニングコストが
低減される。
In the drying furnace according to the present invention, for example, when an automobile body coated with a paint containing an organic solvent is carried into the furnace body and heated, the coating film is dried and hardened. At this time, since the exposed surface of the furnace body and the inner surface of the duct through which the air in the furnace body flows are coated with a water electrolysis accelerating material obtained by kneading a pyroelectric material powder with a heat-resistant inorganic adhesive, When the pyroelectric material is heated, a negative charge appears on the exposed surface in the furnace or the inner surface of the duct due to the pyroelectric effect. On the other hand, when the work is heated, moisture and organic solvent evaporate from the undried coating film,
With the convection of the air in the furnace, this adheres and aggregates on the exposed surface and the inner surface of the duct to form a dust. The molecules of water contained in the tar can receive electrons appearing by pyroelectric effect, some of, H 2 O + 2e - → O 2- + H 2 H 2 O + e - → O - + the reaction represented by H 2, is electrolyzed into hydrogen and ionized oxygen. Then, the ionized oxygen reacts with an organic substance which is a main component of the tar adhering to the exposed surface in the furnace, oxidizes it, and decomposes it into water and carbon dioxide.
Accordingly, since the tar attached to the exposed surface in the furnace body is gradually decomposed and reduced in weight, the frequency and labor of the cleaning work are reduced, and the load on the exhaust gas treatment device is also reduced. , Running costs are reduced.

【0008】 さらに、本発明に係る他の乾燥炉は、炉
体内の表出面、もしくは、炉体内の空気が流通するダク
トの内面に、放射性元素を含むセラミック粉末を耐熱性
の無機接着剤に混練した酸素活性化材が塗工されてい
る。この乾燥炉によれば、炉体内の表出面などに塗工さ
れた酸素活性化材に含まれる放射性元素から、炉体内の
表出面やダクトの内面に付着凝集したヤニに含まれる水
の分子に放射線が照射されて、その一部は、 3H2 O → O3 + 3H2 2H2 O → O2 + 2H2 で表される反応により水が水素と酸素に分離されて、酸
素やオゾンが得られる。したがって、これらの酸素やオ
ゾンが、ヤニの主成分である有機物と反応し、これを酸
化して水と二酸化炭素に分解するので、炉体内の表出面
やダクトの内面に付着したヤニが徐々に分解されて減量
される。
Further, in another drying furnace according to the present invention, a ceramic powder containing a radioactive element is kneaded with a heat-resistant inorganic adhesive on an exposed surface in a furnace or on an inner surface of a duct through which air flows in the furnace. Oxygen activator is applied. According to this drying furnace, water molecules contained in the tar attached and coagulated on the exposed surface of the furnace and the inner surface of the duct are converted from radioactive elements contained in the oxygen activator coated on the exposed surface of the furnace, etc. radiation is irradiated, some of which are separated 3H 2 O → O 3 + 3H 2 2H 2 O → O 2 + 2H reaction with water is hydrogen and oxygen that is represented by 2, resulting oxygen and ozone Can be Therefore, these oxygen and ozone react with the organic matter which is the main component of the tar, oxidize it and decompose it into water and carbon dioxide, and the tar adhering to the exposed surface in the furnace and the inner surface of the duct gradually disappears. Decomposed and reduced in weight.

【0009】[0009]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて具体的に説明する。図1は本発明に係る乾燥
炉を示す説明図、図2は炉体内での化学変化を示す模式
図である。なお、説明の都合上、図1において、右側が
暗赤パネルで炉体内を加熱する輻射加熱ゾーン、左側が
熱風を吹き出させて炉体内を加熱する対流加熱ゾーンを
示す。
Embodiments of the present invention will be specifically described below with reference to the drawings. FIG. 1 is an explanatory view showing a drying furnace according to the present invention, and FIG. 2 is a schematic view showing a chemical change in the furnace. For convenience of explanation, in FIG. 1, the right side shows a radiant heating zone for heating the inside of the furnace with a dark red panel, and the left side shows a convection heating zone for blowing the hot air to heat the inside of the furnace.

【0010】 本例に係る乾燥炉1は、自動車ボディの
塗装用乾燥炉として用いられるもので、塗装ブース(図
示せず)に連続して設けられ、炉体2内には、ワークW
となる自動車ボディを搬送するコンベア3がその長手方
向に沿って敷設されている。そして、乾燥炉1の前段側
には、未乾燥塗膜を生乾き状態まで乾燥させる輻射加熱
ゾーン4Aが形成され、その後段側に、輻射加熱ゾーン
4Aで乾燥された塗膜を焼付乾燥する対流加熱ゾーン4
Bが形成されている。
The drying furnace 1 according to the present embodiment is used as a drying furnace for coating an automobile body, and is provided continuously to a coating booth (not shown).
A conveyor 3 for transporting an automobile body is laid along the longitudinal direction. A radiant heating zone 4A for drying the undried coating film to a completely dry state is formed on the front side of the drying furnace 1, and a convection heating for baking and drying the coating film dried in the radiant heating zone 4A is provided on the subsequent stage. Zone 4
B is formed.

【0011】 輻射加熱ゾーン4Aには、熱風発生装置
5から熱風が循環供給される暗赤パネル6が配設されて
おり、この暗赤パネル6の輻射熱により炉体2内が加熱
される。また、対流加熱ゾーン4Bには、熱風吸込ダク
ト7から吸い込まれた熱風を、熱交換器8で加熱した
後、熱風吹出ダクト9から吹き出させる熱風循環系10
が形成され、その炉体2内には、熱風吹出ダクト9から
吹き出した熱風の横流れを防止するゲート型の仕切壁2
Pが所定間隔で形成されている。なお、12は炉体2内
で発生した汚染空気を排出する排ガス吸込ダクト、13
は排ガス吸込ダクト12を介して排出された汚染空気
(排ガス)を浄化処理する排ガス処理装置である。
The radiant heating zone 4 A is provided with a dark red panel 6 to which hot air is circulated and supplied from a hot air generator 5, and the inside of the furnace body 2 is heated by the radiant heat of the dark red panel 6. In the convection heating zone 4B, a hot air circulating system 10 for heating hot air sucked from the hot air suction duct 7 by the heat exchanger 8 and then blowing it out of the hot air blowing duct 9 is provided.
Are formed in the furnace body 2, and a gate-type partition wall 2 for preventing the hot air blown out from the hot air blowing duct 9 from flowing laterally.
P is formed at predetermined intervals. Reference numeral 12 denotes an exhaust gas suction duct for discharging contaminated air generated in the furnace body 2;
Reference numeral denotes an exhaust gas treatment device for purifying contaminated air (exhaust gas) discharged through the exhaust gas suction duct 12.

【0012】 そして、炉体2内の左右側壁2L及び2
R,天井壁2U,床壁2F,仕切壁2P,暗赤パネル6
の外面,熱風吸込ダクト7及び熱風吹出ダクト9の外面
などの炉体2内の表出面14や、熱風循環系10の各ダ
クト7,9及び排ガス吸込ダクト12の内面15には、
焦電材料の粉末を耐熱性の無機接着剤に混練した水電解
促進材16が塗工されている
Then, the left and right side walls 2 L and 2 in the furnace body 2
R, ceiling wall 2U, floor wall 2F, partition wall 2P, dark red panel 6
, Outer surfaces of the hot-air suction duct 7 and the hot-air outlet duct 9, etc., inside the furnace body 2, each of the ducts 7 and 9 of the hot-air circulation system 10, and an inner surface 15 of the exhaust gas suction duct 12.
A water electrolysis accelerator 16 obtained by kneading a pyroelectric material powder with a heat-resistant inorganic adhesive is applied.

【0013】 ここで、焦電材料としては、例えば、ト
ルマリン(電気石)や、石英(SiO2 )や、タンタル
酸リチウム(LiTaO3 )や、チタン酸鉛(PbTi
3 )や、PZT磁器(チタン酸ジルコン酸鉛:PbZ
rO3 とPbTiO3 の固溶体)など、乾燥炉の炉内温
度で焦電作用を生ずる任意のものを採用することができ
る。また、石英(SiO2 )に、長石,ジルコン(Zr
SiO4 )及び酸化チタン(TiO2 )のうち1種以上
のものを混合した混合粉末でもよい。これら焦電材料
は、いずれも乾燥炉の雰囲気温度程度に加熱されたとき
に焦電効果を示し、その表面に電荷が表れる。
Here, examples of the pyroelectric material include tourmaline (tourmaline), quartz (SiO 2 ), lithium tantalate (LiTaO 3 ), and lead titanate (PbTi).
O 3 ), PZT porcelain (lead zirconate titanate: PbZ)
Any material that produces a pyroelectric effect at the temperature inside the drying furnace, such as a solid solution of rO 3 and PbTiO 3 , can be employed. Also, feldspar and zircon (Zr) were added to quartz (SiO 2 ).
A mixed powder obtained by mixing at least one of SiO 4 ) and titanium oxide (TiO 2 ) may be used. Each of these pyroelectric materials exhibits a pyroelectric effect when heated to about the ambient temperature of a drying furnace, and charges appear on the surface.

【0014】 なお、水電解促進材16を構成する無機
接着剤としては、水ガラスや、コロイダルシリカ、コロ
イダルアルミナ等の低温処理(500℃)で結合強度を
発揮する耐熱性の無機系接着剤が用いられる。そして、
上述した焦電材料の粉末を耐熱性の前記無機接着剤に混
練した水電解促進材16が、炉体2内の表出面14及び
炉体2内の空気が流通するダクト7,9,12の内面1
5を構成する鋼板17の表面に10μm〜1mmの厚さ
で塗工されている。塗工する方法は、エア霧化による吹
き付けであっても、ロールコーターなどによりコーティ
ングする場合であってもよい。なお、水電解促進材16
と鋼板17の熱膨張係数が異なるので、水電解促進材1
6を厚めに塗工する場合は、鋼板17の全面に均一に塗
工せずに、不連続に塗工しておけば、鋼板17が熱膨張
しても水電解促進材16がひび割れするおそれがない。
As the inorganic adhesive constituting the water electrolysis accelerating material 16, a heat-resistant inorganic adhesive which exhibits a bonding strength in a low-temperature treatment (500 ° C.) such as water glass or colloidal silica or colloidal alumina is used. Used. And
The water electrolysis accelerating material 16 obtained by kneading the above pyroelectric material powder with the heat-resistant inorganic adhesive is used to form the exposed surface 14 in the furnace body 2 and the ducts 7, 9, 12 through which the air in the furnace body 2 flows. Inner surface 1
5 is coated on the surface of the steel plate 17 with a thickness of 10 μm to 1 mm. The method of coating may be spraying by air atomization or coating with a roll coater or the like. The water electrolysis accelerator 16
And the steel plate 17 have different thermal expansion coefficients.
When the coating 6 is applied thickly, if the coating is not applied uniformly to the entire surface of the steel plate 17 but is applied discontinuously, the water electrolysis promoter 16 may be cracked even if the steel plate 17 is thermally expanded. There is no.

【0015】 以上が本発明の一例構成であって、次に
その作用を説明する。乾燥炉1を起動させて、炉体2内
が所定の乾燥温度まで上昇したところで、ワークWとな
る自動車ボディをコンベア3で搬送し、その塗膜を乾燥
する。このとき、塗膜に含まれる水分や有機溶剤が蒸発
して、炉体2内の空気の対流に伴って、天井壁2U,左
右側壁2R及び2L,床壁2F,仕切壁2P,暗赤パネ
ル6の外面,熱風吸込ダクト7及び熱風吹出ダクト9の
外面などの炉体2内の表出面14に付着凝集したり、熱
風循環系10の各ダクト7,9や、排ガス吸込ダクト1
2を流通してその内面15に付着凝集してヤニとなる。
The above is an example of the configuration of the present invention, and its operation will be described below. When the drying furnace 1 is started and the inside of the furnace body 2 rises to a predetermined drying temperature, the automobile body to be the work W is conveyed by the conveyor 3 and the coating film is dried. At this time, the moisture and the organic solvent contained in the coating film evaporate, and the convection of the air in the furnace body 2 causes the ceiling wall 2U, the left and right side walls 2R and 2L, the floor wall 2F, the partition wall 2P, the dark red panel. 6 and the outer surfaces of the hot-air suction duct 7 and the hot-air outlet duct 9 such as the outer surfaces of the hot-air blow-out duct 9.
2 circulates and adheres and agglomerates on the inner surface 15 thereof to form tar.

【0016】 一方、炉体2内の表出面14や、各ダク
ト7,9,12の内面15には、焦電材料の粉末を耐熱
性の無機接着剤に混練した水電解促進材16が塗工され
ており、これに含まれる焦電材料が加熱されたときに、
その焦電効果により、炉体2内の表出面14や、ダクト
7,9,12の内面15に電荷が表れる。ここで、表出
面14やダクト12の内面15に付着したヤニに含まれ
る水の分子は、水電解促進材16の表面に表れた電子を
受け取って、その一部は、 H2 O +2e- → O2- + H2 2 O + e- → O- + H2 で表される反応により、水素とイオン化された酸素に電
気分解される。そして、このイオン化された酸素が、炉
体2内の表出面14等に付着しているヤニの主成分であ
る有機物と反応し、これを酸化して水と二酸化炭素に分
解していく。
On the other hand, the exposed surface 14 in the furnace 2 and the inner surface 15 of each of the ducts 7, 9, 12 are coated with a water electrolysis accelerating material 16 obtained by kneading a pyroelectric material powder with a heat-resistant inorganic adhesive. When the pyroelectric material contained therein is heated,
Due to the pyroelectric effect, charges appear on the exposed surface 14 in the furnace body 2 and on the inner surfaces 15 of the ducts 7, 9, and 12. Here, the water molecules contained in the tar attached to the exposed surface 14 and the inner surface 15 of the duct 12 receive the electrons appearing on the surface of the water electrolysis accelerating material 16, and a part thereof is H 2 O + 2e → O 2− + H 2 H 2 O + e → O + H 2 is used to electrolyze into hydrogen and ionized oxygen. Then, the ionized oxygen reacts with an organic substance, which is a main component of the tar attached to the exposed surface 14 and the like in the furnace body 2, and oxidizes this to decompose into water and carbon dioxide.

【0017】 したがって、炉体2内の表出面14やダ
クト12の内面14に付着したヤニが徐々に分解されて
減量されていくので、その分、清掃作業の頻度及び労力
が軽減されると共に、排ガス処理装置13の負荷も軽減
されて、メンテナンスコスト,ランニングコストが低減
される。
Accordingly, since the tar adhering to the exposed surface 14 in the furnace body 2 and the inner surface 14 of the duct 12 is gradually decomposed and reduced in weight, the frequency and labor of the cleaning operation are reduced accordingly, and The load on the exhaust gas treatment device 13 is also reduced, and maintenance costs and running costs are reduced.

【0018】 また、炉体2内の表出面14及びダクト
7,9,12の内面15に、前記水電解促進材16に替
えて、放射性元素を含むセラミック粉末を耐熱性の無機
接着剤に混練した酸素活性化材18を塗工する場合であ
ってもよい。放射性元素としては、トリウム(Th),
ウラン(U),アクチニウム(Ac),ネプツニウム
(Np)などが用いられる。
In place of the water electrolysis promoter 16, ceramic powder containing a radioactive element is kneaded with a heat-resistant inorganic adhesive on the exposed surface 14 in the furnace body 2 and the inner surfaces 15 of the ducts 7, 9, and 12. It may be a case in which the applied oxygen activator 18 is applied. Thorium (Th),
Uranium (U), actinium (Ac), neptunium (Np) and the like are used.

【0019】 この場合、炉体2内の表出面14などに
塗工された酸素活性化材に含まれる放射性元素から、炉
体2内の表出面14やダクト12の内面15に付着凝集
したヤニに含まれる水の分子に放射線が照射されて、そ
の一部は、 3H2 O → O3 + 3H2 2H2 O → O2 + 2H2 で表される反応により水が水素と酸素に分離されて、酸
素やオゾンが得られる。したがって、これらの酸素やオ
ゾンが、ヤニの主成分である有機物と反応し、これを酸
化して水と二酸化炭素に分解するので、炉体2内の表出
面14やダクト12の内面15に付着したヤニが徐々に
分解されて減量される。
In this case, from the radioactive element contained in the oxygen activator applied to the exposed surface 14 and the like in the furnace body 2, the dust adhered and coagulated on the exposed surface 14 in the furnace body 2 and the inner surface 15 of the duct 12. and radiation is irradiated to a molecule of water contained in, some of the water is separated into hydrogen and oxygen by the reaction expressed by 3H 2 O → O 3 + 3H 2 2H 2 O → O 2 + 2H 2 To obtain oxygen and ozone. Therefore, these oxygen and ozone react with the organic matter which is the main component of the tar, oxidize and decompose it into water and carbon dioxide, and adhere to the exposed surface 14 in the furnace body 2 and the inner surface 15 of the duct 12. The dried tarnish is gradually decomposed and reduced in weight.

【0020】 なお、焦電材料の粉末を耐熱性の前記無
機接着剤に混練した水電解促進材16や、放射性元素を
含むセラミック粉末を耐熱性の無機接着剤に混練した酸
素活性化材18を塗工するのに替えて、焦電材料の粉末
を混練して焼成したセラミックで形成された水電解促進
タイルや、放射性元素を含むセラミックで形成された酸
素活性化タイルを無機接着剤などで貼設した場合であっ
てもよい。このように、タイルにしておけば、工業的に
タイルを製造することにより、その品質を一定に維持す
ることができ、また、タイルを貼るだけでよいので、施
工が簡単で、塗工する場合に比して塗りムラを起こすこ
とがなく、誰でも均一に仕上げることができるというメ
リットがある。なお、この場合、タイル目地にヤニが詰
まらないように、耐熱性,弾力性のある充填剤を充填す
ることが望ましい。
A water electrolysis accelerator 16 in which pyroelectric material powder is kneaded with the heat-resistant inorganic adhesive, and an oxygen activating material 18 in which ceramic powder containing a radioactive element is kneaded with heat-resistant inorganic adhesive are used. Instead of coating, paste a water electrolysis promotion tile made of ceramic that is obtained by kneading and firing a pyroelectric material powder, or an oxygen-activated tile made of ceramic containing a radioactive element with an inorganic adhesive or the like. May be provided. In this way, if the tiles are used, the quality can be maintained at a constant level by manufacturing the tiles industrially. There is an advantage in that no coating unevenness occurs and anyone can finish uniformly. In this case, it is desirable to fill the tile joint with a heat-resistant and elastic filler so that the joint is not clogged.

【0021】[0021]

【発明の効果】以上述べたように、本発明によれば、炉
体内の表出面やダクトの内面に付着したヤニに含まれる
水分が水素と酸素に分解されて、その酸素により、ヤニ
の主成分となる有機物が酸化されて水と二酸化炭素に分
解されるので、表出面などに付着したヤニが自然に減量
化されていき、清掃作業の頻度や労力を軽減すると同時
に、排ガス処理装置の負荷を軽減してランニングコス
ト,メンテナンスコストを低減することができるという
大変優れた効果を奏する。
As described above, according to the present invention, the moisture contained in the tar attached to the exposed surface in the furnace and the inner surface of the duct is decomposed into hydrogen and oxygen, and the oxygen is used to separate the water from the tar. Organic components are oxidized and decomposed into water and carbon dioxide.As a result, the amount of tar attached to the surface is reduced naturally, reducing the frequency and effort of cleaning work, and at the same time reducing the load on exhaust gas treatment equipment. This leads to a very excellent effect that running costs and maintenance costs can be reduced.

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

【図1】 本発明に係る乾燥炉を示す説明図。FIG. 1 is an explanatory view showing a drying furnace according to the present invention.

【図2】 炉体内での化学変化を示す模式図。FIG. 2 is a schematic view showing a chemical change in a furnace.

【符号の説明】[Explanation of symbols]

1・・・乾燥炉 2・・・炉体 W・・・ワーク 7・・・熱風吸込ダクト 9・・・熱風吹出ダクト 14・・・炉体内の表出面 15・・・ダクトの内面 16・・・水電解促進材 18・・・酸素活性化材 DESCRIPTION OF SYMBOLS 1 ... Drying furnace 2 ... Furnace body W ... Work 7 ... Hot air suction duct 9 ... Hot air blowing duct 14 ... Surface in furnace body 15 ... Inner surface of duct 16 ...・ Water electrolysis promoter 18 ・ ・ ・ Oxygen activator

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 炉体(2)内でワーク(W)を乾燥する
ことにより蒸発有機溶剤を含む汚染空気が生成される乾
燥炉において、炉体(2)内の表出面(14)、もしく
は、炉体(2)内の空気が流通するダクト(7, 9, 12)の
内面 (15) に、焦電材料の粉末を耐熱性の無機接着剤に
混練した水電解促進材(16)が塗工されていることを特徴
とする乾燥炉。
1. A drying furnace in which contaminated air containing an evaporated organic solvent is generated by drying a work (W) in a furnace body (2), an exposed surface (14) in the furnace body (2), or On the inner surface (15) of the duct (7, 9, 12) through which air flows in the furnace body (2), a water electrolysis accelerator (16) obtained by kneading pyroelectric material powder with a heat-resistant inorganic adhesive is used. A drying oven characterized by being coated.
【請求項2】 炉体(2)内でワーク(W)を乾燥する
ことにより蒸発有機溶剤を含む汚染空気が生成される乾
燥炉において、炉体(2)内の表出面(14)、もしく
は、炉体(2)内の空気が流通するダクト(7, 9, 12)の
内面 (15) に、放射性元素を含むセラミック粉末を耐熱
性の無機接着剤に混練した酸素活性化材(18) が塗工さ
れていることを特徴とする乾燥炉。
2. A drying furnace in which contaminated air containing an evaporated organic solvent is generated by drying a work (W) in a furnace body (2), a surface (14) in the furnace body (2), or An oxygen activator (18) in which ceramic powder containing a radioactive element is kneaded with a heat-resistant inorganic adhesive on the inner surface (15) of a duct (7, 9, 12) through which air in the furnace body (2) flows. A drying oven, characterized by being coated.
【請求項3】 炉体(2)内でワーク(W)を乾燥する
ことにより蒸発有機溶剤を含む汚染空気が生成される乾
燥炉において、炉体(2)内の表出面(14)、もしく
は、炉体(2)内の空気が流通するダクト(7, 9, 12)の
内面 (15) に、焦電材料の粉末を混練して焼成したセラ
ミックで形成された水電解促進タイルが貼設されている
ことを特徴とする乾燥炉。
3. A drying furnace in which contaminated air containing an evaporating organic solvent is generated by drying a work (W) in a furnace body (2), a surface (14) in the furnace body (2), or A water electrolysis promotion tile made of ceramics obtained by kneading and firing a pyroelectric material powder is attached to the inner surface (15) of a duct (7, 9, 12) through which air flows in the furnace body (2). A drying oven, characterized in that it has been made.
【請求項4】 炉体(2)内でワーク(W)を乾燥する
ことにより蒸発有機溶剤を含む汚染空気が生成される乾
燥炉において、炉体(2)内の表出面(14)、もしく
は、炉体(2)内の空気が流通するダクト(7, 9, 12)の
内面 (15) に、放射性元素を含むセラミックで形成され
た酸素活性化タイルが貼設されていることを特徴とする
乾燥炉。
4. A drying furnace in which contaminated air containing an evaporated organic solvent is generated by drying a work (W) in a furnace body (2), an exposed surface (14) in the furnace body (2), or An oxygen-activated tile made of ceramic containing a radioactive element is attached to an inner surface (15) of a duct (7, 9, 12) through which air flows in a furnace body (2). Drying oven.
JP04477398A 1998-02-26 1998-02-26 drying furnace Expired - Fee Related JP3655461B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04477398A JP3655461B2 (en) 1998-02-26 1998-02-26 drying furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04477398A JP3655461B2 (en) 1998-02-26 1998-02-26 drying furnace

Publications (2)

Publication Number Publication Date
JPH11248347A true JPH11248347A (en) 1999-09-14
JP3655461B2 JP3655461B2 (en) 2005-06-02

Family

ID=12700741

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04477398A Expired - Fee Related JP3655461B2 (en) 1998-02-26 1998-02-26 drying furnace

Country Status (1)

Country Link
JP (1) JP3655461B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106091661A (en) * 2016-06-08 2016-11-09 河北盛联节能科技有限公司 System for coupling and drying slurry-like heat-insulating material by using flue gas waste heat
CN109078788A (en) * 2018-09-19 2018-12-25 黄河科技学院 A kind of automotive lacquer house exhaust processing unit
CN110612423A (en) * 2017-06-16 2019-12-24 株式会社大气社 Coating drying furnace

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106091661A (en) * 2016-06-08 2016-11-09 河北盛联节能科技有限公司 System for coupling and drying slurry-like heat-insulating material by using flue gas waste heat
CN110612423A (en) * 2017-06-16 2019-12-24 株式会社大气社 Coating drying furnace
CN110612423B (en) * 2017-06-16 2020-12-25 株式会社大气社 Coating drying furnace
CN109078788A (en) * 2018-09-19 2018-12-25 黄河科技学院 A kind of automotive lacquer house exhaust processing unit
CN109078788B (en) * 2018-09-19 2020-12-29 沈菊青 Exhaust treatment device for automobile paint spraying workshop

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