JPH035836Y2 - - Google Patents

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Publication number
JPH035836Y2
JPH035836Y2 JP12543785U JP12543785U JPH035836Y2 JP H035836 Y2 JPH035836 Y2 JP H035836Y2 JP 12543785 U JP12543785 U JP 12543785U JP 12543785 U JP12543785 U JP 12543785U JP H035836 Y2 JPH035836 Y2 JP H035836Y2
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JP
Japan
Prior art keywords
furnace
heat
heating
heat medium
section
Prior art date
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Expired
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JP12543785U
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Japanese (ja)
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JPS6232995U (en
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Publication of JPS6232995U publication Critical patent/JPS6232995U/ja
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Description

【考案の詳細な説明】 産業上の利用分野 本考案は、ワーク(工作物)の乾燥等に利用さ
れる間接加熱式熱風循環炉の改良に関するもので
ある。
[Detailed Description of the Invention] Industrial Application Field The present invention relates to an improvement of an indirect heating type hot air circulation furnace used for drying workpieces, etc.

従来の技術 この種の炉は、従来第2図で示されるような構
成となつている。この図にいて、符号1,2,3
はワーク(図示せず)の通路に沿つて設置された
作業炉であり、ワークはこの中を矢印方向へ進行
しつつ乾燥処理される。この乾燥には熱風が利用
され、該熱風が循環させるための熱風循環路4,
5,6が各作業炉1,2,3に設けられている。
符号7,8,9は熱風を循環させるためのフアン
である。
2. Description of the Related Art This type of furnace has conventionally been constructed as shown in FIG. In this figure, the numbers 1, 2, 3
is a working furnace installed along the path of the workpiece (not shown), and the workpiece is dried while traveling in the direction of the arrow. Hot air is used for this drying, and a hot air circulation path 4 for circulating the hot air;
5 and 6 are provided in each of the working furnaces 1, 2, and 3.
Reference numerals 7, 8, and 9 are fans for circulating hot air.

また、、上記各熱風循環路4,5,6には各々
熱媒循環路10,11,12が付設され、各熱媒
循環路10,11,12には熱媒加熱部であるバ
ーナ13,14,15及び燃焼炉16,17,1
8が設けられている。また熱媒を循環させるため
のフアン19,20,21も設けられている。な
お、符号22,23,24は排ガスダンパであ
る。
Further, each of the hot air circulation paths 4, 5, and 6 is provided with a heat medium circulation path 10, 11, and 12, respectively, and each heat medium circulation path 10, 11, and 12 is provided with a burner 13, which is a heat medium heating section. 14, 15 and combustion furnace 16, 17, 1
8 is provided. Fans 19, 20, and 21 are also provided for circulating the heat medium. Note that numerals 22, 23, and 24 are exhaust gas dampers.

上記各熱風循環路4,5,6と各熱媒循環路1
0,11,12との所定の接点箇所には熱媒であ
る燃焼ガスから風に対して熱を与えるための熱交
換器25,26,27が設けられている。
Each of the above hot air circulation paths 4, 5, 6 and each heat medium circulation path 1
Heat exchangers 25, 26, and 27 are provided at predetermined points of contact with the wind turbines 0, 11, and 12 to provide heat from combustion gas, which is a heat medium, to the wind.

しかして、燃焼炉16,17,18内でバーナ
13,14,15からの燃料が燃焼されると、そ
の燃焼ガスがフアン19,20,21の作用で各
熱媒循環路10,11,12中を矢印方向に循環
し、また同時に熱風循環路4,5,6内において
も風がフアン7,8,9によつて矢印方向に流
れ、その間熱交換器25,26,27によつて熱
媒から熱を受けて熱風となり、各作業炉1,2,
3内を経由する。作業炉1,2,3内にて該熱風
はワークに当り乾燥等の作業を行なうものであ
る。
When the fuel from the burners 13, 14, 15 is burned in the combustion furnaces 16, 17, 18, the combustion gas is transferred to each heat medium circulation path 10, 11, 12 by the action of the fans 19, 20, 21. At the same time, air flows in the direction of the arrow in the hot air circulation paths 4, 5, and 6 by fans 7, 8, and 9, while the heat exchangers 25, 26, and 27 generate heat. It receives heat from the medium and becomes hot air, which blows into each work furnace 1, 2,
Go through 3. The hot air hits the workpieces in the work furnaces 1, 2, and 3 and performs operations such as drying.

また、第2図において符号28,29,30は
作業炉1,2,3中の雰囲気ガスを捕集し脱臭装
置31に導くためのダクトである。符号32,3
3,34は各ダクト28,29,30に設けられ
たダンパである。脱臭装置31は上記雰囲気ガス
を燃焼室35と、該燃焼室35内に燃料と新鮮空
気を送り込んで燃焼させるための脱臭用バーナ3
6とを備えている。符号37はフアンであり、上
記ダクト28,29,30から来るガスはこのフ
アン37により上記燃焼室35中に圧送される。
また符号38は熱交換器であり、上記ダクト2
8,29,30からのガスはここで予熱された
後、フアン37で燃焼室35に送られるようにな
つている。
Further, in FIG. 2, reference numerals 28, 29, and 30 are ducts for collecting the atmospheric gas in the working furnaces 1, 2, and 3 and guiding it to the deodorizing device 31. code 32,3
3 and 34 are dampers provided in each duct 28, 29, and 30. The deodorizing device 31 includes a combustion chamber 35 for the atmospheric gas, and a deodorizing burner 3 for feeding fuel and fresh air into the combustion chamber 35 for combustion.
6. Reference numeral 37 is a fan, and the gas coming from the ducts 28, 29, 30 is forced into the combustion chamber 35 by this fan 37.
Further, reference numeral 38 is a heat exchanger, and the duct 2
Gases from 8, 29, and 30 are preheated here and then sent to a combustion chamber 35 by a fan 37.

しかして、各作業炉1,2,3内で塗装等の焼
付乾燥がなされると、その際HC成分、ヤニ等が
炉内に発生するが、これらを含む雰囲気ガスはそ
の一部がダクト28,29,30を通つて上記脱
臭装置31に至り、該ガス中に含まれる有害成分
の燃焼除去がなされる。このような処理を終えた
ガスは無臭状態で排気ダクト39から装置外へ排
出され、またこれにより作業炉内のHC成分等の
希釈化がなされ濃縮化が防止される。
However, when baking and drying of paint etc. is carried out in each work furnace 1, 2, 3, HC components, tar, etc. are generated in the furnace, and some of the atmospheric gas containing these is transferred to the duct 28. , 29, and 30, the gas reaches the deodorizing device 31, where harmful components contained in the gas are burned and removed. The gas that has undergone such treatment is discharged out of the apparatus from the exhaust duct 39 in an odorless state, and this dilutes the HC components in the working furnace and prevents them from concentrating.

第3図は、他の従来例を示している。なお、こ
の図は作図の便宜上単一の作業炉1部分を抜き出
して示しているが、上記従来例と異なり、直燃脱
臭炉40を各作業炉1,2,3に対して備えてい
る。この脱臭炉40は作業炉1からその中の雰囲
気ガスを一部取り出す捕集ダクト41を備え、そ
の流れ方向に沿つてフアン42、バーナ43、上
記脱臭炉40、熱交換器44を配置してなるもの
である。
FIG. 3 shows another conventional example. Although this figure shows a single working furnace 1 portion extracted for convenience of drawing, a direct combustion deodorizing furnace 40 is provided for each of the working furnaces 1, 2, and 3, unlike the conventional example described above. This deodorizing furnace 40 includes a collection duct 41 for taking out a part of the atmospheric gas therein from the working furnace 1, and a fan 42, a burner 43, the deodorizing furnace 40, and a heat exchanger 44 are arranged along the flow direction of the collection duct 41. It is what it is.

しかして、作業炉1内の雰囲気ガスはフアン4
2の回転により捕集ダクト41中に引き込まれ、
バーナ43より燃料と共に脱臭炉40中に噴出さ
れる。炉内において雰囲気ガス中の有害成分は火
炎及び高温雰囲気(通常700℃以上)により燃焼
除去され排ガスダクト47から排出される。な
お、作業炉1内から排出された雰囲気ガス量に相
当する新鮮な外気が導管45から熱交換器46を
経て作業炉中に供給される。
Therefore, the atmospheric gas inside the working furnace 1 is
2 is drawn into the collection duct 41,
It is ejected from the burner 43 into the deodorizing furnace 40 together with the fuel. In the furnace, harmful components in the atmospheric gas are burned and removed by flame and high temperature atmosphere (usually 700° C. or higher) and are discharged from the exhaust gas duct 47. Note that fresh outside air corresponding to the amount of atmospheric gas discharged from the inside of the working furnace 1 is supplied into the working furnace from the conduit 45 via the heat exchanger 46.

考案が解決しようとする問題点 しかしながら、上記従来の循環炉は前者のもの
にあつては燃焼系と別に脱臭装置31を取り付け
なければならないので、大きなスペースを占有
し、イニシヤルコストが非常に高くなる。さら
に、脱臭処理のためのランニングコストが別に必
要となるという問題を有している。
Problems to be solved by the invention However, in the case of the former type of conventional circulation furnace, a deodorizing device 31 must be installed separately from the combustion system, which occupies a large space and has a very high initial cost. Become. Furthermore, there is a problem in that running costs for deodorizing treatment are required separately.

また、後者のものにあつては各作業炉1,2,
3毎に脱臭炉40等を設けなければならないとい
う欠点を有する。
In addition, in the case of the latter, each work furnace 1, 2,
The disadvantage is that a deodorizing furnace 40 etc. must be provided for every 3.

問題点を解決するための手段 本考案は上記問題点を解決するため、所定箇所
に熱媒加熱部を有する熱媒循環路と、所定箇所に
各作業炉を有する複数の熱風循環路とを備え、両
循環路の所定の接点箇所に上記風が上記熱媒から
熱を受け取るための熱交換器が設けられた間接加
熱式熱風循環炉において、上記熱媒循環路の熱媒
加熱部は1箇所のみ設けられると共に該熱媒は液
体とされ、かつ熱媒循環路は熱媒加熱部と上記各
熱交換器との間に形成され、さらに所定の作業炉
と熱媒加熱部の燃焼部との間を連絡して作業炉内
の雰囲気ガスを上記燃焼部に導く捕集路が設けら
れた構成を採用している。
Means for Solving the Problems In order to solve the above problems, the present invention includes a heat medium circulation path having a heat medium heating section at a predetermined location, and a plurality of hot air circulation paths each having a working furnace at a predetermined location. In the indirect heating type hot air circulation furnace, in which a heat exchanger for the wind to receive heat from the heating medium is provided at a predetermined contact point of both circulation paths, the heating medium heating section of the heating medium circulation path is provided at one location. The heating medium is liquid, and the heating medium circulation path is formed between the heating medium heating section and each heat exchanger, and the heating medium circulation path is formed between the heating medium heating section and the combustion section of the heating medium heating section. A configuration is adopted in which a collection path is provided that communicates between the combustion chambers and guides the atmospheric gas within the working furnace to the combustion section.

作 用 熱媒循環路の熱媒としてガスでなく液体が用い
られている。また、その加熱部は1箇所である。
このため熱媒循環路及びその周辺は小型化され、
占有スペースも小さくなつている。
Function A liquid is used as the heating medium in the heating medium circuit, rather than a gas. Moreover, there is only one heating section.
For this reason, the heat medium circulation path and its surroundings have been downsized,
The space it occupies is also getting smaller.

炉の稼動に際して炉中で生じた雰囲気ガスは捕
集路を通つて熱媒加熱部の燃焼部に至る。ここ
で、雰囲気ガス中の有害成分は燃焼され、雰囲気
ガスは無臭状態になつて排出される。また、これ
により作業炉内でのHC成分等の濃縮化が防止さ
れる。
Atmospheric gas generated in the furnace during operation of the furnace reaches the combustion section of the heat medium heating section through a collection path. Here, harmful components in the atmospheric gas are burned, and the atmospheric gas is discharged in an odorless state. Furthermore, this prevents concentration of HC components and the like within the working furnace.

実施例 第1図は本考案の一実施例を示している。な
お、これらの図において第2図及び第3図におけ
ると同一構成をとるものについては同一符号を付
する。
Embodiment FIG. 1 shows an embodiment of the present invention. In these figures, parts having the same configuration as in FIGS. 2 and 3 are given the same reference numerals.

第1図で示されるように、熱媒加熱部48は1
箇所のみ設けられている。また、熱媒も気体では
なくて液体である油が使用されている。熱媒加熱
部48はボイラであり、該ボイラにはバーナ4
9、排気ダクト50等が付設されている。
As shown in FIG. 1, the heat medium heating section 48 has one
Only certain locations are provided. Furthermore, the heat medium used is not gas, but oil, which is a liquid. The heat medium heating section 48 is a boiler, and the boiler includes a burner 4.
9, an exhaust duct 50 etc. are attached.

上記熱媒加熱部48と各熱媒循環路4,5,6
の熱交換器51,52,53との間には熱媒循環
路54,55,56が並列的に形成されており、
各往路には電磁弁などの制御弁57,58,59
が設置されている。また所定箇所にはポンプ60
が設置されている。これらの制御弁57,58,
59はすべて制御部(図示せず)によつて制御さ
れるようになつており、制御部はタイマ等を備
え、作業炉1,2,3の起動に際してワークの流
れの上流側に位置する作業炉1に対応した制御弁
57から順次下流側の制御弁58,59に向けて
経時的に開動作させるよう構成されている。一つ
の制御弁の開動作から次の弁の開動作に至るまで
の時間Tは一つの作業炉の立上り時間とほぼ一致
している。
The heat medium heating section 48 and each heat medium circulation path 4, 5, 6
Heat medium circulation paths 54, 55, 56 are formed in parallel between the heat exchangers 51, 52, 53,
Control valves 57, 58, 59 such as solenoid valves are provided on each outward path.
is installed. In addition, a pump 60 is installed at a specified location.
is installed. These control valves 57, 58,
59 are all controlled by a control section (not shown), and the control section is equipped with a timer, etc., and when starting up the work furnaces 1, 2, and 3, the workpieces located on the upstream side of the workpiece flow are controlled by a control section (not shown). It is configured to sequentially open the control valves 58 and 59 downstream from the control valve 57 corresponding to the furnace 1 over time. The time T from the opening operation of one control valve to the opening operation of the next valve almost coincides with the start-up time of one working furnace.

しかして、作業炉1,2,3の始動に際して
は、熱媒加熱部48であるボイラが稼動され、熱
媒の加熱がなされる。この熱媒たる油は比熱が
424(Kcal/m3,℃)であり、従来の熱媒たる空
気の0.30(Kcal/m3・℃)の約1,400倍にあた
り、それ故、熱媒循環路55,56,57の配
管、ポンプ60は従来のものに比べ格段に小型化
されている。また、熱交換器51,52,53も
従来の気体−気体方式に対して気体−液体方式と
なり、熱通過率(Kcal/m3・h・℃)が約2倍
になるため従来の大きさの半分程度のものを使用
し得るものである。
Thus, when starting up the working furnaces 1, 2, and 3, the boiler, which is the heating medium heating section 48, is operated to heat the heating medium. This heating medium, oil, has a specific heat of
424 (Kcal/m 3 , ℃), which is approximately 1,400 times the 0.30 (Kcal/m 3 ℃) of air, which is a conventional heating medium. , the pump 60 is much smaller than conventional pumps. In addition, the heat exchangers 51, 52, and 53 are also gas-liquid type compared to the conventional gas-gas type, and the heat transfer rate (Kcal/ m3・h・℃) is approximately twice as large as the conventional size. About half of that can be used.

次いで、制御部からの信号に基づき、制御弁5
9が開かれ、熱媒が熱交換器51に至り、一方フ
アン7の作動による風が熱風循環路4中を循環し
つつ熱交換器51で熱を受け取り作業炉1内を加
熱する。この制御弁57のみが開かれる時間Tは
この作業炉1の立ち上り時間に相当し、このTを
できるだけ短縮するためのバーナ49の容量は、
この間標準稼動時の該作業炉1の負荷をQとすれ
ば例えば2Qに設定される。この作業炉1内の温
度が所定の高さに立ち上れば、制御部の図示しな
い検知器により検知されさらに次の制御弁58が
開かれる。
Next, based on the signal from the control section, the control valve 5
9 is opened and the heat medium reaches the heat exchanger 51, while the air generated by the operation of the fan 7 circulates in the hot air circulation path 4 and receives heat in the heat exchanger 51 to heat the inside of the working furnace 1. The time T during which only the control valve 57 is open corresponds to the start-up time of the working furnace 1, and the capacity of the burner 49 to shorten this T as much as possible is:
If the load of the working furnace 1 during standard operation during this period is Q, it is set to, for example, 2Q. When the temperature inside the working furnace 1 rises to a predetermined level, it is detected by a detector (not shown) in the control section, and the next control valve 58 is opened.

この結果、下流側の隣接作業炉2に2Qの熱量
が加えられるようバーナ49の容量が 2Q+Q=3Qとして調節され、該炉2も時間T
の間はより多く加熱されて立ち上り時間の短縮化
がなされる。時間Tが経過すると、さらに次の制
御弁59が開かれる。
As a result, the capacity of the burner 49 is adjusted as 2Q+Q=3Q so that 2Q of heat is added to the adjacent work furnace 2 on the downstream side, and the furnace 2 is also
During this time, more heat is generated and the rise time is shortened. After time T has elapsed, the next control valve 59 is opened.

その結果、さらに下流側の作業炉3に2Qの熱
量が加えられるようにバーナ49の容量が2Q+
Q+Q=4Qとして調節され、該炉3も時間Tの
間より多く加熱されて立ち上り時間の短縮化がな
される。時間Tが経過するとバーナ49の容量は
3Qに調整され、作業炉3は負荷3Qの標準稼動状
態とされて、ワークの炉1,2,3内への搬入が
開始されることとなる。
As a result, the capacity of the burner 49 is increased to 2Q+ so that 2Q of heat is added to the work furnace 3 further downstream.
Adjustment is made such that Q+Q=4Q, and the furnace 3 is also heated more during time T to shorten the rise time. After time T passes, the capacity of burner 49 becomes
The work furnace 3 is adjusted to 3Q, and the work furnace 3 is brought into a standard operating state with a load of 3Q, and the workpieces are started to be carried into the furnaces 1, 2, and 3.

第1図における符号61,62は作業炉1,3
と熱媒加熱部48の燃焼部であるバーナ49との
間を連絡するダクトである。このダクト61,6
2は作業炉1,3内の雰囲気ガスをバーナ49に
導くための雰囲気ガスの捕集器である。その途中
には雰囲気ガスを捕集するためのフアン63が設
けられている。
Reference numerals 61 and 62 in FIG. 1 indicate the working furnaces 1 and 3.
This is a duct that communicates between the burner 49 and the burner 49 which is the combustion section of the heat medium heating section 48. This duct 61,6
Reference numeral 2 denotes an atmospheric gas collector for guiding the atmospheric gas in the working furnaces 1 and 3 to the burner 49. A fan 63 for collecting atmospheric gas is provided in the middle.

このため、雰囲気ガスはバーナ49に送られて
燃焼ガスと混合され熱媒加熱部48で燃焼され
る。これにより雰囲気ガス中のHC成分等は燃焼
除去され、雰囲気ガスは無臭無害となつて排気ダ
クト50より外界へ排出される。また、各作業炉
1,2,3内ではこれにより有害成分の高濃度化
が防止されることとなる。
Therefore, the atmospheric gas is sent to the burner 49, mixed with combustion gas, and burned in the heat medium heating section 48. As a result, HC components and the like in the atmospheric gas are burned and removed, and the atmospheric gas becomes odorless and harmless and is discharged to the outside world from the exhaust duct 50. In addition, this prevents harmful components from increasing in concentration within each of the working furnaces 1, 2, and 3.

また、符号64は新鮮な空気の供給ダクトであ
り、上記排気ダクト50に設置された熱交換器6
5を経て作業炉2に至つている。
Further, reference numeral 64 is a fresh air supply duct, and a heat exchanger 6 installed in the exhaust duct 50
5 to the working furnace 2.

これにより、各作業炉1,2,3から排出され
た雰囲気ガスと同量の気体が逆に作業炉1,2,
3内に至り、各作業炉1,2,3内の無臭無害化
を促進することとなる。なお、ダクト61及びダ
クト62は作業炉2にも接続しても良いものであ
る。
As a result, the same amount of atmospheric gas discharged from each work furnace 1, 2, and 3 is transferred to the work furnaces 1, 2, and 3.
3, thereby promoting the deodorization and detoxification of the inside of each working furnace 1, 2, and 3. Note that the duct 61 and the duct 62 may also be connected to the work furnace 2.

考案の効果 本考案は以上のような構成及び作用からなるの
で、熱媒加熱部48、熱媒循環路54,55,5
6熱交換器51,52,53等の小型化をなし
得、従つて、間接加熱式熱風循環炉全体の構成を
簡素にし、占有スペースの減少、該熱損失等の設
備の固定損失の低減を図り得るものである。そし
て、脱臭装置として熱媒加熱部48の燃焼部を使
用しているので、従来の燃焼系とは別体として脱
臭装置31を設ける方式、また各作業炉1,2,
3毎に設ける方式に比して、さらに占有スペース
の低減化を図りうるものである。さらに、このよ
うに小型化を図りうることから、加熱・脱臭に要
するエネルギーの低減化をも図りうるものであ
る。
Effects of the invention Since the present invention has the above-described configuration and operation, the heating medium heating section 48, the heating medium circulation paths 54, 55, 5
6 The heat exchangers 51, 52, 53, etc. can be downsized, and the overall configuration of the indirect heating hot air circulation furnace can be simplified, occupying space, and fixed losses of equipment such as heat loss can be reduced. It is possible. Since the combustion section of the heat medium heating section 48 is used as the deodorizing device, the deodorizing device 31 is provided separately from the conventional combustion system, and each work furnace 1, 2,
Compared to the method of providing every third section, the space occupied can be further reduced. Furthermore, since it can be made smaller in this way, it is also possible to reduce the energy required for heating and deodorizing.

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

第1図は本考案に係る間接加熱式熱風循環炉の
ブロツク回路図であり、第2図は従来例のものの
ブロツク回路図、第3図は他の従来例のものの一
部を取り出したブロツク回路図である。 1,2,3……作業炉、48……熱媒加熱部、
49……バーナ、54,55,56……熱媒循環
路、61,62……捕集路。
Fig. 1 is a block circuit diagram of an indirect heating type hot air circulation furnace according to the present invention, Fig. 2 is a block circuit diagram of a conventional example, and Fig. 3 is a block circuit diagram of a part of another conventional example. It is a diagram. 1, 2, 3... Working furnace, 48... Heat medium heating section,
49... Burner, 54, 55, 56... Heat medium circulation path, 61, 62... Collection path.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 所定箇所に熱媒加熱部を有する熱媒循環路と、
所定箇所に各作業炉を有する複数の熱風循環路と
を備え、両循環路の所定の接点箇所に上記風が上
記熱媒から熱を受け取るための熱交換器が設けら
れた間接加熱式熱風循環炉において、上記熱媒循
環路の熱媒加熱部は1箇所のみ設けられると共に
該熱媒は液体とされ、かつ熱媒循環路は熱媒加熱
部と上記各熱交換器との間に形成され、さらに所
定の作業炉と熱媒加熱部の燃焼部との間を連絡し
て作業炉内の雰囲気ガスを上記燃焼部に導く捕集
路が設けられたことを特徴とする間接加熱式熱風
循環炉。
a heating medium circulation path having a heating medium heating section at a predetermined location;
An indirect heating hot air circulation system comprising a plurality of hot air circulation paths each having a working furnace at a predetermined location, and a heat exchanger for the air to receive heat from the heating medium at a predetermined contact point between the two circulation paths. In the furnace, the heat medium heating section of the heat medium circulation path is provided at only one location, the heat medium is in liquid form, and the heat medium circulation path is formed between the heat medium heating section and each of the heat exchangers. , an indirect heating type hot air circulation characterized in that a collection path is further provided that connects a predetermined working furnace and a combustion section of the heat medium heating section and guides atmospheric gas in the working furnace to the combustion section. Furnace.
JP12543785U 1985-08-15 1985-08-15 Expired JPH035836Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12543785U JPH035836Y2 (en) 1985-08-15 1985-08-15

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12543785U JPH035836Y2 (en) 1985-08-15 1985-08-15

Publications (2)

Publication Number Publication Date
JPS6232995U JPS6232995U (en) 1987-02-26
JPH035836Y2 true JPH035836Y2 (en) 1991-02-14

Family

ID=31018337

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12543785U Expired JPH035836Y2 (en) 1985-08-15 1985-08-15

Country Status (1)

Country Link
JP (1) JPH035836Y2 (en)

Also Published As

Publication number Publication date
JPS6232995U (en) 1987-02-26

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