JPH032021B2 - - Google Patents

Info

Publication number
JPH032021B2
JPH032021B2 JP3818685A JP3818685A JPH032021B2 JP H032021 B2 JPH032021 B2 JP H032021B2 JP 3818685 A JP3818685 A JP 3818685A JP 3818685 A JP3818685 A JP 3818685A JP H032021 B2 JPH032021 B2 JP H032021B2
Authority
JP
Japan
Prior art keywords
rotary furnace
hot air
furnace
coating
granules
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.)
Expired
Application number
JP3818685A
Other languages
Japanese (ja)
Other versions
JPS61197909A (en
Inventor
Hiroshi Eiki
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP3818685A priority Critical patent/JPS61197909A/en
Publication of JPS61197909A publication Critical patent/JPS61197909A/en
Publication of JPH032021B2 publication Critical patent/JPH032021B2/ja
Granted legal-status Critical Current

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  • Gasification And Melting Of Waste (AREA)
  • Incineration Of Waste (AREA)
  • Coating Apparatus (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は被除去物に付着した塗装物質を熱分解
により除去するようにした塗装物質除去装置に関
する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a coating substance removal device that removes coating substances adhering to objects to be removed by thermal decomposition.

〔従来技術〕[Prior art]

一般に吹付け塗装する場合には、被塗装物を金
属製の塗装用治具に保持させて塗装しているが、
塗装用治具は被塗装物とともに塗装状態となるた
めに使用回数を重ねるに従つて塗装物質が表面に
厚く付着して使用に支障を来たすことになる。そ
こで、従来では、表面に塗装物質が付着した被除
去物たる塗装用治具を例えばバツチ式焼却炉に投
入し、塗装用治具の表面に付着した塗装物質を焼
却して取除くようにしている。
Generally, when spray painting, the object to be painted is held in a metal painting jig.
Since the coating jig is in a coating state along with the object to be coated, the more times it is used, the thicker the coating substance will adhere to the surface, which will impede its use. Therefore, in the past, the coating jig, which is the object to be removed and which has coating substances adhered to its surface, was put into a batch-type incinerator, for example, and the coating substances attached to the surface of the coating jig were incinerated and removed. There is.

しかしながら、斯かる従来技術では、焼却炉内
で塗装物質が高温度で燃焼するために焼却炉内の
温度を制御することが困難であることから、焼却
炉内の温度が極めて高くなつて金属性の塗装用治
具に熱歪が生じ易く再使用が不可能となる場合が
あり、また、焼却後の塗装用治具の表面には焼却
された塗装物質の残渣が付着し、冷却後に塗装用
治具から残渣をブラシ等でこすり落す作業が必要
になるという欠点があつた。
However, with such conventional technology, it is difficult to control the temperature inside the incinerator because the coating material burns at a high temperature in the incinerator. Painting jigs tend to undergo thermal distortion and may become impossible to reuse, and the surface of the painting jigs after incineration is coated with residues of the incinerated coating material, and after cooling, painting jigs may not be able to be used again. The drawback was that it required scrubbing off the residue from the jig with a brush or the like.

〔発明の目的〕[Purpose of the invention]

本発明は上記の点に鑑みてなされたもので、そ
の目的は、被除去物に熱歪が生ずることを防止し
得、また、被除去物の表面に付着する塗装物質の
残渣を除去する作業をなくし得て作業効率を高め
得る塗装物質除去装置を提供するにある。
The present invention has been made in view of the above points, and its purpose is to prevent the occurrence of thermal distortion on the object to be removed, and to remove the residue of coating substances adhering to the surface of the object to be removed. An object of the present invention is to provide a coating substance removing device that can eliminate the problem and improve work efficiency.

〔発明の要約〕[Summary of the invention]

本発明は、多数のセラミツク製粒状体を収容し
てなり略水平な軸線の周りに回転される回転炉
と、この回転炉の内周壁に設けられ該回転炉の回
転にともなつて前記粒状体を掻上げて落下させる
掻上部材と、前記回転炉内に熱風を供給する熱風
供給装置とを具備しているところに特徴を有す
る。
The present invention relates to a rotary furnace that accommodates a large number of ceramic granules and rotates around a substantially horizontal axis, and a rotary furnace that is provided on an inner circumferential wall of the rotary furnace and that rotates the granules as the rotary furnace rotates. The rotary furnace is characterized in that it includes a scraping member that scrapes up and drops the rotary furnace, and a hot air supply device that supplies hot air into the rotary furnace.

〔実施例〕〔Example〕

以下本発明の第1の実施例につき第1図乃至第
3図を参照して説明する。
A first embodiment of the present invention will be described below with reference to FIGS. 1 to 3.

先ず、塗装物質除去装置について第1図及び第
2図に従い述べる。1は基台であり、2はこの基
台1上に後述するように設置される略長円筒状の
回転炉である。この回転炉2の内部には多数のセ
ラミツク製粒状体3が収容されており、これらの
多数の粒状体3は、回転炉2の内周壁に略全長に
わたつて断続的に取付けられた断面が略L字形の
多数の掻上部材4によつて、回転炉2の矢印5方
向への回転に伴い掻上げられ落下させられる。6
は塗装物質の付着した被除去物であり、これは、
回転炉2の両端部内に複数本の支持アーム7を介
して支持された筒状の支持部材8(右端部のみ図
示)に挿入支持されている。9は回転炉2の一端
部を被う排気カバーであり、この上面部には排気
ガスを排出する排気筒10が突設され、背面部に
は被除去物6を回転炉2内に対して出し入れする
ための出し入れ口(図示せず)を開閉する扉11
が設けられている。そして、扉11の第2図中右
方部位には被除去物6のための搬出入装置12が
設置されている。13は環状のシール部材であ
り、これは鍔部13aが排気カバー9の右側面部
に取着されることによつて回転炉2の外周部に接
触するようになつている。一方、回転炉2の右端
部の外周部には環状のレール14と鎖車15とが
固定されており、その内のレール14は基台1に
固定された支持台16の回転自在な支持ローラ1
7に支持されている。この場合、図示はしない
が、回転炉2の左端部側にもレール14、支持台
16及び支持ローラ17と同様のレール、支持台
及び支持ローラが設けられており、以て回転炉2
が基台1に、その軸方向が略水平になるようにし
て回転自在に設置されている。尚、支持ローラ1
7及び支持台16は第1図に示すように夫々左、
右一対設けられており、しかも支持ローラ17の
ん両側には鍔部18,18が形成されていて、回
転炉2の軸方向及び第1図における左、右方向へ
の移動を規制している。19はモータ、減速機構
等からなる駆動装置であり、その駆動軸20には
小鎖車21が固定されており、この小鎖車21と
前記鎖車15との間にチエーン22が張設され、
以て、駆動軸20の回転が小鎖車21、チエーン
22及び鎖車15を介して回転炉2に矢印5方向
の回転として伝達されるようになつている。
First, the coating substance removal device will be described with reference to FIGS. 1 and 2. 1 is a base, and 2 is a substantially long cylindrical rotary furnace installed on the base 1 as described later. A large number of ceramic granules 3 are housed inside the rotary furnace 2, and these many granules 3 have cross-sections that are intermittently attached to the inner circumferential wall of the rotary furnace 2 over approximately the entire length. As the rotary furnace 2 rotates in the direction of arrow 5, it is scraped up and dropped by a large number of roughly L-shaped scraping members 4. 6
is the object to be removed to which the coating substance has adhered, and this is
It is inserted and supported by a cylindrical support member 8 (only the right end is shown) which is supported within both ends of the rotary furnace 2 via a plurality of support arms 7 . Reference numeral 9 denotes an exhaust cover that covers one end of the rotary furnace 2. An exhaust pipe 10 for discharging exhaust gas is provided on the upper surface of the exhaust cover 9, and an exhaust pipe 10 for discharging exhaust gas is provided on the back surface of the exhaust cover 9 to cover one end of the rotary furnace 2. A door 11 that opens and closes an inlet/outlet (not shown) for loading and unloading.
is provided. A loading/unloading device 12 for the object 6 to be removed is installed on the right side of the door 11 in FIG. Reference numeral 13 denotes an annular sealing member, and a flange 13a of this is attached to the right side surface of the exhaust cover 9, so that it comes into contact with the outer circumference of the rotary furnace 2. On the other hand, an annular rail 14 and a chain wheel 15 are fixed to the outer periphery of the right end of the rotary furnace 2, and the rail 14 is a rotatable support roller of a support stand 16 fixed to the base 1. 1
It is supported by 7. In this case, although not shown, a rail, a support stand, and a support roller similar to the rail 14, support stand 16, and support roller 17 are provided on the left end side of the rotary furnace 2, so that the rotary furnace 2
is rotatably installed on the base 1 so that its axial direction is substantially horizontal. In addition, support roller 1
7 and the support stand 16 are respectively on the left side and the support stand 16 as shown in FIG.
A right pair is provided, and flanges 18, 18 are formed on both sides of the support roller 17 to restrict movement of the rotary furnace 2 in the axial direction and in the left and right directions in FIG. . Reference numeral 19 denotes a drive device consisting of a motor, a speed reduction mechanism, etc. A small chain wheel 21 is fixed to its drive shaft 20, and a chain 22 is stretched between the small chain wheel 21 and the chain wheel 15. ,
Thus, the rotation of the drive shaft 20 is transmitted to the rotary furnace 2 via the small chain wheel 21, the chain 22, and the chain wheel 15 as rotation in the direction of the arrow 5.

さて、塗装物質除去装置を含むシステム全体の
構成を第3図に従つて述べる。23は略円筒状の
熱風供給装置であり、これの一端部(左端部)に
は加熱装置としての第1のバーナー24が配設さ
れており、内部には図示しないターボ送風器が設
けられている。そして、熱風供給装置23は、該
ターボ送風機が外部から吸引した空気とバーナー
24からの熱とから高速の熱風を生成して他端部
から前記排気カバー9と略同様の構成の吸気カバ
ー9′を介して回転炉2へ供給するようになつて
いる。25はサイクロン集塵機であり、これは回
転炉2から排気筒10を介して排出される排気ガ
スの中から熱分解された付着塗装物質の残渣を分
離するものである。26はサイクロン集塵機25
からの排気ガスを熱交換機27の一方の流通路を
介して燃焼炉28へ送り込む押込フアンである。
そして、燃焼炉28の一端部には加熱装置として
の第2のバーナー29が配設されており、他端部
から排出される排気ガスは熱交換機27の他方の
流通路を介して湿式スクラバー30に送り込まれ
る。この湿式スクラバー30の内部には図示はし
ないが湿式のフイルタが設けられており、下方部
位には水タンク31が配設されている。尚、熱交
換機27の他方の流通路を経た排気の一部は押込
フアン32によつて熱風供給装置23内に送り込
まれるようになつている。33は誘引フアンであ
り、これは湿式スクラバー30から排気ガスを吸
引し、これを煙突34に送り込み外部へ排出する
ものである。
Now, the configuration of the entire system including the coating substance removal device will be described with reference to FIG. 23 is a substantially cylindrical hot air supply device, and a first burner 24 as a heating device is disposed at one end (left end) of this, and a turbo blower (not shown) is provided inside. There is. Then, the hot air supply device 23 generates high-speed hot air from the air sucked in from the outside by the turbo blower and the heat from the burner 24, and supplies it from the other end to an intake cover 9' having substantially the same configuration as the exhaust cover 9. It is designed to be supplied to the rotary furnace 2 via. 25 is a cyclone dust collector, which separates the residue of the thermally decomposed coating material from the exhaust gas discharged from the rotary furnace 2 through the exhaust stack 10. 26 is cyclone dust collector 25
This is a forced fan that sends the exhaust gas from the heat exchanger 27 to the combustion furnace 28 through one of the flow paths of the heat exchanger 27.
A second burner 29 as a heating device is disposed at one end of the combustion furnace 28, and the exhaust gas discharged from the other end is passed through the other flow path of the heat exchanger 27 to the wet scrubber 30. sent to. Although not shown, a wet filter is provided inside the wet scrubber 30, and a water tank 31 is provided in the lower part. A portion of the exhaust gas that has passed through the other flow path of the heat exchanger 27 is sent into the hot air supply device 23 by a force fan 32. Reference numeral 33 denotes an induction fan, which sucks exhaust gas from the wet scrubber 30, sends it into the chimney 34, and discharges it to the outside.

次に上記構成の作用を説明する。被除去物6は
本実施例では例えば自動車塗装用台車があるが、
これには自動車を載置支持するために支持用の凹
凸部、金具類が精密に設けられており、熱歪を生
じさせてはならないものである。そして、被除去
物6に付着した塗装物質は、ビニール系、アクリ
ル系或いはポリエステル系等の主として有機高分
子物質からなる基材に着色剤として顔料、染料等
の無機物が加えられ、更に硬化剤、安定剤及び可
塑剤並びに溶剤が加えられたもので、これが塗装
後の乾燥及び焼付処理等によつて内部に含まれた
溶剤がほとんど蒸発した状態となつて固体化して
被除去物6の表面に付着している。このような塗
装物質の付着した被除去物6が搬出入装置12か
ら扉11を開放した排気カバー9を通じて回転炉
2内へ搬入され、支持部材8によつて支持され
る。そして、扉11を閉塞し、第1のバーナー2
4に点火し図示しないターボ送風機を作動させる
ことによつて、熱風供給装置23から550℃〜600
℃の熱風を生成させ、この熱風を回転炉2へ供給
させるとともに、駆動装置19を作動させて回転
炉2を矢印5方向へ例えば1分間に30回転させ
る。この結果、回転炉2に供給された熱風は回転
炉2に収容されたセラミツク製粒状体3を加熱
し、加熱されたセラミツク製粒状体3は遠赤外線
を放射して被除去物6を加熱する。更に、回転炉
2が回転することによりセラミツク製粒状体3が
掻上部材4によつて掻上げられ被除去物6の上に
落下するので、該粒状体3は被除去物6の周りに
一様に衝突する。そして、該粒状体3の放射する
遠赤外線の熱エネルギーと熱風との相乗作用によ
つて、被除去物6の表面に付着した塗装物質が表
面部から順次熱分該(クラツキング)され、熱分
解により可燃性の気体(例えばCHn、H2等)が
発生するが、セラミツク製粒状体3が被除去物6
の周りに順次均一に存在するので、その遮断作用
及び熱風の速度により可燃性の気体が発火される
ことが防止され、可燃性の気体は熱風に混合され
る。一方、塗装物質が熱分解された後の被除去物
6の表面には残渣が生ずるが、掻上部材4によつ
て落下させられたセラミツク製粒状体3がたえず
被除去物6の表面に衝突するので、残渣は被除去
物6の表面から剥離されて熱風に混合される。そ
の後、可燃性の気体と残渣とが混合された排気ガ
スは押込フアン26の吸引作用によりサイクロン
集塵機25へ入る。ここで、残渣だけが除去さ
れ、可燃性の気体は排気ガスに混合された状態で
押込フアン26の吸引作用により熱交換機27の
一方の流通路を介して燃焼炉28へ至る。この燃
焼炉28は第2のバーナー29によつて内部の温
度が700℃程度になるように制御されており、燃
焼炉28内に入つた可燃性の気体は第2のバーナ
ー29の炎によつて発火され燃焼炉28内で完全
燃焼される。その後、燃焼炉28からの排気ガス
の一部は押込フアン32によつて吸引され熱交換
機27の他方の流通路を介して熱風供給装置23
へ供給される。また、熱交換機27の他方の流通
路を経た排気ガスの残りは誘引フアン33によつ
て吸引された湿式スクラバー30を通過する。こ
の通過時に排気ガスはその中に含まれている粉塵
及び媒煙等が捕獲された後煙突34から外部へ排
出される。
Next, the operation of the above configuration will be explained. In this embodiment, the object to be removed 6 is, for example, an automobile painting trolley.
This is precisely provided with supporting unevenness and metal fittings for mounting and supporting the automobile, and must not cause thermal distortion. The coating substance adhering to the object to be removed 6 is obtained by adding an inorganic substance such as a pigment or dye as a coloring agent to a base material mainly made of an organic polymer material such as vinyl, acrylic, or polyester, and further adding a hardening agent, Stabilizers, plasticizers, and solvents are added to this product, and when it is dried and baked after painting, most of the solvent contained inside has evaporated, solidified, and is applied to the surface of the object to be removed 6. It's attached. The object to be removed 6 with the coating substance adhered to it is carried into the rotary furnace 2 from the carry-in/out device 12 through the exhaust cover 9 with the door 11 open, and is supported by the support member 8 . Then, the door 11 is closed and the first burner 2 is closed.
By igniting 4 and operating a turbo blower (not shown), the temperature of 550°C to 600°C is supplied from the hot air supply device 23.
℃ hot air is generated, this hot air is supplied to the rotary furnace 2, and the drive device 19 is operated to rotate the rotary furnace 2 in the direction of the arrow 5, for example, 30 times per minute. As a result, the hot air supplied to the rotary furnace 2 heats the ceramic granules 3 housed in the rotary furnace 2, and the heated ceramic granules 3 emit far infrared rays to heat the object 6 to be removed. . Furthermore, as the rotary furnace 2 rotates, the ceramic granules 3 are scraped up by the scraping member 4 and fall onto the object 6 to be removed, so that the granules 3 surround the object 6 to be removed. collide like that. Due to the synergistic effect of the far-infrared thermal energy emitted by the granular material 3 and the hot air, the coating material adhering to the surface of the object 6 to be removed is thermally cracked (cracking) from the surface part and thermally decomposed. combustible gas (for example, CHn, H2, etc.) is generated, but the ceramic granules 3 are removed from the object 6.
Because of its uniform presence in sequence around the air, its blocking action and the speed of the hot air prevent the flammable gas from being ignited, and the flammable gas is mixed into the hot air. On the other hand, after the coating material is thermally decomposed, a residue is generated on the surface of the object to be removed 6, but the ceramic granules 3 dropped by the scraping member 4 constantly collide with the surface of the object to be removed 6. Therefore, the residue is peeled off from the surface of the object 6 to be removed and mixed with the hot air. Thereafter, the exhaust gas mixed with flammable gas and residue enters the cyclone dust collector 25 by the suction action of the forcing fan 26. Here, only the residue is removed, and the flammable gas is mixed with the exhaust gas and reaches the combustion furnace 28 through one of the flow passages of the heat exchanger 27 by the suction action of the forcing fan 26. This combustion furnace 28 is controlled by a second burner 29 so that the internal temperature is approximately 700°C, and the flammable gas that has entered the combustion furnace 28 is blown by the flame of the second burner 29. It is then ignited and completely combusted in the combustion furnace 28. Thereafter, a part of the exhaust gas from the combustion furnace 28 is sucked in by the forced fan 32 and passed through the other flow path of the heat exchanger 27 to the hot air supply device 23.
supplied to Further, the remainder of the exhaust gas that has passed through the other flow path of the heat exchanger 27 passes through the wet scrubber 30 that is sucked in by the induction fan 33. During this passage, the exhaust gas is discharged to the outside from the chimney 34 after the dust and smoke contained therein are captured.

このような本実施例によれば、次のような効果
を得ることができる。即ち、塗装物質の付着した
被除去物6を回転炉2内に収納支持し、回転炉2
内に550℃〜600℃に加熱した高速度の熱風を供給
するとともに、回転炉2を1分間に30回転させて
回転炉2に収納されたセラミツク製粒状体3を掻
上部材4によつて掻上げ被除去物6上に落下させ
るようにし、以て、被除去物6に付着した塗装物
質を熱分解させて熱分解により発生した可燃性の
気体が回転炉2内で発火しないようにしたので、
従来のバツチ式焼却炉で焼却した場合とは異な
り、被除去物6に熱歪が生ずることもなくなり、
被除去物6の再使用がすべて可能となる。また、
回転炉2を1分間に30回転させて回転炉2内に収
納されたセラミツク製粒状体3を掻上部材4によ
り掻上げて被除去物6上に落下させるようにした
ので、熱分解により生じた残渣を被除去物6から
自動的に剥離除去させることができ、従来とは異
なり被除去物から冷却後ブラシ等で残渣をこすり
落とすような作業を行う必要がなくなり、作業効
率を高め得る。更に、回転炉2内で発生した可燃
性で有害な気体を燃焼炉28内で燃焼させるよう
にしたので、黒煙及び有害ガスの放出等の大気汚
染問題を解決できる。しかも、燃焼炉28からの
酸素濃度の極めて低い排気ガスの一部を熱風供給
装置23に供給するようにしたので、回転炉2内
に供給される熱風は酸素濃度の低い且つ高速度の
ものとなり、従つて、回転炉2内での発火を一層
抑制できるものであり、所期の目的を充分に達成
できるものである。
According to this embodiment, the following effects can be obtained. That is, the object to be removed 6 to which the coating substance has adhered is housed and supported in the rotary furnace 2, and the rotary furnace 2
While supplying high-velocity hot air heated to 550°C to 600°C, the rotary furnace 2 is rotated 30 times per minute to scrape the ceramic granules 3 stored in the rotary furnace 2 with the scraping member 4. The scraped material was dropped onto the object 6 to be removed, thereby thermally decomposing the coating material adhering to the object 6 to be removed, and preventing the flammable gas generated by the thermal decomposition from igniting in the rotary furnace 2. So,
Unlike the case of incineration in a conventional batch type incinerator, there is no thermal distortion in the object 6 to be removed.
All of the objects 6 to be removed can be reused. Also,
Since the rotary furnace 2 is rotated 30 times per minute and the ceramic granules 3 housed in the rotary furnace 2 are scraped up by the scraping member 4 and dropped onto the object 6 to be removed, the ceramic granules 3 are removed by thermal decomposition. The residue can be automatically peeled off and removed from the object to be removed 6, and unlike the conventional method, there is no need to perform work such as scrubbing the residue off the object to be removed with a brush or the like after cooling, and work efficiency can be improved. Furthermore, since the flammable and harmful gases generated in the rotary furnace 2 are combusted in the combustion furnace 28, air pollution problems such as the release of black smoke and harmful gases can be solved. Moreover, since a part of the exhaust gas with extremely low oxygen concentration from the combustion furnace 28 is supplied to the hot air supply device 23, the hot air supplied into the rotary furnace 2 has a low oxygen concentration and high velocity. Therefore, ignition within the rotary furnace 2 can be further suppressed, and the intended purpose can be fully achieved.

第4図は本発明の第2の実施例を示すもので、
前記実施例と同一部分には同一符号を付して説明
を省略し、以下異なる部分についてのみ説明す
る。即ち、35は回転炉2を正逆回転させるため
の駆動装置であり、36は掻上部材4と対称な形
状即ち逆L字形の掻上部材で、これは回転炉2の
逆回転たる矢印5方向とは反転方向の回転時にセ
ラミツク製粒状体3を掻上げ落下させるものであ
る。従つて、第2の実施例においては第1の実施
例よりも一層セラミツク製粒状体3を被除去物6
に均一に落下させ得る利点がある。
FIG. 4 shows a second embodiment of the present invention,
The same parts as in the previous embodiment are given the same reference numerals and the explanation thereof will be omitted, and only the different parts will be explained below. That is, 35 is a drive device for rotating the rotary furnace 2 in forward and reverse directions, and 36 is a scraping member having a shape symmetrical to the scraping member 4, that is, an inverted L-shape, which corresponds to the arrow 5 indicating the reverse rotation of the rotary furnace 2. The direction means that when rotating in the reverse direction, the ceramic granules 3 are scraped up and dropped. Therefore, in the second embodiment, the ceramic granules 3 are placed more closely to the object to be removed 6 than in the first embodiment.
It has the advantage of being able to fall evenly.

尚、上記各実施例では、回転炉2に供給する熱
風の温度を550℃〜600℃になるように温度制御し
たが、熱風の温度及び速度は被除去物6に付着し
た塗装物質の種類に応じて回転炉2内で該塗装物
質が熱分解され且つ熱分解によつて発生した可燃
性の気体が発火しないようになし得るように適宜
選定すればよい。
In each of the above embodiments, the temperature of the hot air supplied to the rotary furnace 2 was controlled to be 550°C to 600°C, but the temperature and speed of the hot air may vary depending on the type of coating substance attached to the object 6. Accordingly, it may be selected as appropriate so that the coating material is thermally decomposed in the rotary furnace 2 and the flammable gas generated by the thermal decomposition is not ignited.

その他、本発明は上記し且つ図面に示す実施例
にのみ限定されるものではなく、例えば被除去物
としては塗装に用いる器具であれば良い等、要旨
を逸脱しない範囲内で適宜変形して実施し得るこ
とは勿論である。
In addition, the present invention is not limited to the embodiments described above and shown in the drawings, and may be implemented with appropriate modifications within the scope of the gist, for example, the object to be removed may be an instrument used for painting. Of course it is possible.

〔発明の効果〕〔Effect of the invention〕

本発明は以上の説明から明らかなように、回転
炉内に多数のセラミツク製粒状体を収容し、該回
転炉の回転にともなつて回転炉の内周壁に設けら
れた掻上部材が前記粒状体を掻上げて落下させる
ようにし、そして、熱風供給装置が前記回転炉内
に熱風を供給するようにしたので、回転炉内に収
納された被除去物に熱歪が生ずることを防止し
得、また、被除去物の表面に生ずる塗装物質の残
渣が自動的に除去されて除去作業が必要でなく、
作業効率を高め得るという効果を奏する。
As is clear from the above description, the present invention accommodates a large number of ceramic granules in a rotary furnace, and as the rotary furnace rotates, a scraping member provided on the inner circumferential wall of the rotary furnace disposes of the granules. Since the body is raised and dropped, and the hot air supply device supplies hot air into the rotary furnace, it is possible to prevent thermal distortion from occurring in the object to be removed stored in the rotary furnace. In addition, the residue of the coating material that occurs on the surface of the object to be removed is automatically removed, eliminating the need for removal work.
This has the effect of increasing work efficiency.

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

第1図乃至第3図は本発明の第1の実施例を示
すもので、第1図は縦断面図、第2図は要部を断
面して示す部分側面図、第3図は全体の処理シス
テムの構成図であり、第4図は本発明の第2の実
施例を示す第1図相当図である。 図面中、1は基台、2は回転炉、3はセラミツ
ク製粒状体、4は掻上部材、6は被除去物、8は
支持部材、23は熱風供給装置、36は掻上部材
を示す。
1 to 3 show a first embodiment of the present invention. FIG. 1 is a longitudinal sectional view, FIG. 2 is a partial side view showing a main part in section, and FIG. 3 is an overall view. 4 is a block diagram of a processing system, and FIG. 4 is a diagram corresponding to FIG. 1 showing a second embodiment of the present invention. In the drawings, 1 is a base, 2 is a rotary furnace, 3 is a ceramic granule, 4 is a scraping member, 6 is an object to be removed, 8 is a support member, 23 is a hot air supply device, and 36 is a scraping member. .

Claims (1)

【特許請求の範囲】[Claims] 1 多数のセラミツク製粒状体を収容してなり略
水平な軸線の周りに回転される回転炉と、この回
転炉の内周壁に設けられ該回転炉の回転にともな
つて前記粒状体を掻上げて落下させる掻上部材
と、前記回転炉内に熱風を供給する熱風供給装置
とを具備し、前記回転炉内に塗装物質の付着した
被除去物を収納した状態で前記回転炉及び熱風供
給装置を作動させるようにしたことを特徴とする
塗装物質除去装置。
1. A rotary furnace that accommodates a large number of ceramic granules and is rotated around a substantially horizontal axis, and a rotary furnace that is provided on the inner circumferential wall of the rotary furnace and scrapes up the granules as the rotary furnace rotates. and a hot air supply device that supplies hot air into the rotary furnace. A paint substance removal device characterized in that it operates.
JP3818685A 1985-02-27 1985-02-27 Coating substance removing device Granted JPS61197909A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3818685A JPS61197909A (en) 1985-02-27 1985-02-27 Coating substance removing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3818685A JPS61197909A (en) 1985-02-27 1985-02-27 Coating substance removing device

Publications (2)

Publication Number Publication Date
JPS61197909A JPS61197909A (en) 1986-09-02
JPH032021B2 true JPH032021B2 (en) 1991-01-14

Family

ID=12518343

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3818685A Granted JPS61197909A (en) 1985-02-27 1985-02-27 Coating substance removing device

Country Status (1)

Country Link
JP (1) JPS61197909A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020006937A (en) * 2000-07-14 2002-01-26 석청기 Shot abrader

Also Published As

Publication number Publication date
JPS61197909A (en) 1986-09-02

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