JPH10153387A - Operating method for atmosphere circulation type continuous heat treatment furnace - Google Patents

Operating method for atmosphere circulation type continuous heat treatment furnace

Info

Publication number
JPH10153387A
JPH10153387A JP31039796A JP31039796A JPH10153387A JP H10153387 A JPH10153387 A JP H10153387A JP 31039796 A JP31039796 A JP 31039796A JP 31039796 A JP31039796 A JP 31039796A JP H10153387 A JPH10153387 A JP H10153387A
Authority
JP
Japan
Prior art keywords
atmosphere
zone
furnace
unit band
heat treatment
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
JP31039796A
Other languages
Japanese (ja)
Other versions
JP2974629B2 (en
Inventor
Hiroshige Nakagawa
博重 中川
Hisafumi Goto
尚史 後藤
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.)
Chugai Ro Co Ltd
Original Assignee
Chugai Ro Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chugai Ro Co Ltd filed Critical Chugai Ro Co Ltd
Priority to JP8310397A priority Critical patent/JP2974629B2/en
Publication of JPH10153387A publication Critical patent/JPH10153387A/en
Application granted granted Critical
Publication of JP2974629B2 publication Critical patent/JP2974629B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Tunnel Furnaces (AREA)
  • Furnace Details (AREA)
  • Re-Forming, After-Treatment, Cutting And Transporting Of Glass Products (AREA)

Abstract

PROBLEM TO BE SOLVED: To enhance thermal efficiency by employing a down flow system for jetting the atmosphere downward through a porous plate and feeding a part of the atmosphere circulated to a specified unit band of a furnace to the unit band side on the side for loading a material to be treated thereby forming a gas flow in the furnace from the final unit band to the starting unit band. SOLUTION: A planar deflector member 41 is set, while inclining toward the side for loading a material to be treated on the bottom of a furnace located directly under the ceiling fan 4 in a unit band 40c. Consequently, a part of the atmosphere blown downward through a porous plate 7 impinges against the deflector member 41 to form a flow directed toward a unit band adjacent to the.loading side. In the unit band 40c, a material is heat treated by blowing the atmosphere at a specified temperature and migrates from the final unit band to the starting unit band and transfers the heat of the atmosphere from the material extracting side to the loading side thus balancing the heat. According to the arrangement, total fuel consumption of the facility 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、特に、ガラス製品
の熱処理に適用される雰囲気循環式連続熱処理炉の操業
方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of operating an atmosphere circulation type continuous heat treatment furnace applied to heat treatment of glass products.

【0002】[0002]

【従来の技術】従来、ガラス製品等の雰囲気循環式連続
熱処理炉は、特公平2−27589号公報に開示の如き
構成となっている。すなわち、図4に示すように、昇温
帯10、均熱帯20、徐冷帯30および冷却帯40とか
ら構成され、処理材はコンベアチェーンあるいはメッシ
ュベルトVによって各帯10,20,30および40を
搬送され、その間に、図5に示すヒートカーブにしたが
って熱処理されるものである。また、前記各帯10,2
0,30および40はさらに複数の単位帯域10a,1
0b…,20a,20b…,30a,30b…および4
0a,40b…からなる。
2. Description of the Related Art Conventionally, an atmosphere circulation type continuous heat treatment furnace for glass products or the like has a structure as disclosed in Japanese Patent Publication No. 2-27589. That is, as shown in FIG. 4, the heating zone 10, the soaking zone 20, the slow cooling zone 30, and the cooling zone 40 are constituted, and the processing materials are divided into belts 10, 20, 30, and 40 by a conveyor chain or a mesh belt V. It is conveyed and, during that, is subjected to a heat treatment according to a heat curve shown in FIG. In addition, each of the bands 10, 2
0, 30, and 40 are a plurality of unit bands 10a, 1
0b ..., 20a, 20b ..., 30a, 30b ... and 4
0a, 40b...

【0003】前記昇温帯10および均熱帯20の各単位
帯域10a,10b…,20a,20b…は、大略、図
6に示すように、耐火断熱材からなる炉本体1の炉内
に、隔壁(バッフル)3と天井ファン(循環ファン)4
と加熱手段であるラジアントチューブバーナ5を配設し
た構成からなる。なお、加熱手段5はラジアントチュー
ブバーナに限らず、電熱ヒータ、直火バーナ等であって
もよい。
Each of the unit zones 10a, 10b,..., 20a, 20b... Of the temperature-raising zone 10 and the soaking zone 20 is, as shown in FIG. Baffle 3 and ceiling fan (circulation fan) 4
And a radiant tube burner 5 as heating means. The heating means 5 is not limited to a radiant tube burner, but may be an electric heater, a direct fire burner, or the like.

【0004】そして、ラジアントチューブバーナ5を燃
焼させるとともに天井ファン4を回転して、炉内雰囲気
を炉壁2と隔壁3との間に形成される循環路6を矢印で
示すように循環させ、ラジアントチューブバーナ5によ
って加熱されて所定温度に加熱された炉内雰囲気を天井
ファン4で吸引撹拌して、多孔板7から下方に吹き付
け、コンベアチェーンあるいはメッシュベルトVにより
搬送される処理材(図示せず)を熱処理するものであ
る。
[0004] Then, the radiant tube burner 5 is burned and the ceiling fan 4 is rotated to circulate the furnace atmosphere through a circulation path 6 formed between the furnace wall 2 and the partition wall 3 as shown by an arrow. The atmosphere inside the furnace heated by the radiant tube burner 5 and heated to a predetermined temperature is sucked and agitated by the ceiling fan 4 and sprayed downward from the perforated plate 7 to be conveyed by a conveyor chain or a mesh belt V (shown in FIG. Is heat-treated.

【0005】なお、徐冷帯30の各単位帯域30a,3
0b…は、図7に示すように、昇温帯10および均熱帯
20の各単位帯域の構成の他に、隔壁3の上方に大気を
導入する給気ダクト31と炉内雰囲気を排出する排気ダ
クト32とを設けたもので、炉内循環雰囲気温度をラジ
アントチューブバーナ5の燃焼量、給気ダクト31から
の大気導入量および排気ダクト32からの炉内雰囲気の
排気量を調節して所定温度にする。
The unit zones 30a, 3a of the slow cooling zone 30
As shown in FIG. 7, reference numerals 0b... Denote the air supply duct 31 for introducing the atmosphere above the partition wall 3 and the exhaust duct for discharging the atmosphere in the furnace, in addition to the configuration of the unit zones of the warming zone 10 and the soaking zone 20. The furnace circulating atmosphere temperature is adjusted to a predetermined temperature by adjusting the combustion amount of the radiant tube burner 5, the amount of air introduced from the air supply duct 31, and the amount of exhaust of the furnace atmosphere from the exhaust duct 32. I do.

【0006】また、冷却帯40の単位帯域40a,40
b…は、図8に示すように、徐冷帯30の単位帯域30
a,30b…と比較すれば明らかなように、ラジアント
チューブバーナ5がなく、かつ、炉本体1が断熱構造と
なっていない点のみが異なる。
The unit bands 40a, 40 of the cooling zone 40
b are unit bands 30 of the slow cooling zone 30 as shown in FIG.
As apparent from comparison with a, 30b,..., the only difference is that there is no radiant tube burner 5 and the furnace body 1 does not have a heat insulating structure.

【0007】そして、各単位帯域10a,10b…,2
0a,20b…,30a,30b…,40a,40b…
の雰囲気温度は、各単位帯域に設けた図示しない熱電対
により独立して制御されるとともに、隣接単位帯域間で
炉気が流入あるいは流出しない状態に保持される。すな
わち、徐冷および冷却では、当該単位帯域での冷却用空
気の供給量と排気量とをほぼ同一に維持して温度制御を
行なっている。
Then, each unit band 10a, 10b...
0a, 20b ..., 30a, 30b ..., 40a, 40b ...
The ambient temperature is independently controlled by a thermocouple (not shown) provided in each unit zone, and is maintained in a state where furnace air does not flow in or out between adjacent unit zones. That is, in the slow cooling and the cooling, the temperature control is performed while maintaining the supply amount and the exhaust amount of the cooling air in the unit band substantially the same.

【0008】[0008]

【発明が解決しようとする課題】このように、各単位帯
域での温度を完全に独立して制御する方式では、炉気の
流れがなく、均熱帯20の高温炉気が昇温帯10の熱源
に使用されず、熱効率が悪いという問題があった。そこ
で、本発明者らは炉気を、炉の終端側単位帯域から始端
側単位帯域に向かって移動させれば熱効率を向上させる
ことができないかについて検討した。検討した結果、図
9に示すように、炉気流量が所定量、たとえば、図9で
は60m3/minとすると、炉の総必要熱量を最小にで
き、従来方法よりも約20%の熱量が低減し、それだけ
熱効率を向上させることができることを知見した。な
お、図9は、炉気流量を変数として熱収支をシュミレー
シヨンすることにより得たものである。したがって、本
発明は従来の雰囲気循環式連続熱処理炉において、簡単
な構成を付加することにより熱効率の良い雰囲気循環式
連続熱処理炉の操業方法を提供することを目的とする。
As described above, in the system in which the temperature in each unit zone is completely independently controlled, there is no flow of furnace gas, and the high-temperature furnace gas in the solitary zone 20 has a heat source in the heating zone 10. And the thermal efficiency is poor. Therefore, the present inventors examined whether the thermal efficiency could be improved by moving the furnace gas from the unit zone on the end side of the furnace toward the unit zone on the start side. As a result of the study, as shown in FIG. 9, when the furnace air flow rate is a predetermined amount, for example, 60 m 3 / min in FIG. 9, the total required calorific value of the furnace can be minimized, and about 20% of the calorific value is smaller than the conventional method. It has been found that the thermal efficiency can be improved accordingly. FIG. 9 is obtained by simulating the heat balance using the furnace air flow rate as a variable. Accordingly, an object of the present invention is to provide a method of operating a conventional atmosphere circulation type continuous heat treatment furnace which has good thermal efficiency by adding a simple structure to a conventional atmosphere circulation type continuous heat treatment furnace.

【0009】[0009]

【課題を解決するための手段】本発明にかかる雰囲気循
環式連続熱処理炉の操業方法は、前記目的を達成するた
めに、昇温帯、均熱帯、徐冷帯および冷却帯を有すると
ともに、前記各帯に天井ファンと炉内隔壁とにより雰囲
気循環路を形成する複数の単位帯域を有する雰囲気循環
式連続熱処理炉において、雰囲気循環を多孔板から下方
に噴出させるダウンフロー方式とするとともに、前記炉
の所定単位帯域に循環雰囲気の一部を処理材装入側の隣
接単位帯域側に流入させて、炉内に最終単位帯域から始
端単位帯域への炉気流れを形成するようにしたものであ
る。また、少なくとも最終単位帯域の炉床部に偏流部材
を設けることにより循環雰囲気の一部を前記隣接単位帯
域側に流入させるようにしてもよい。さらに、少なくと
も最終単位帯域の多孔板下部に偏流板を設けることによ
り循環雰囲気の一部を処理材装入側の隣接単位帯域側に
流入させるようにしてもよく、さらにまた、少なくとも
最終単位帯域の多孔板を傾斜させることにより循環雰囲
気の一部を処理材装入側の隣接単位帯域側に流入させる
ようにしてもよい。
In order to achieve the above object, a method for operating an atmosphere circulation type continuous heat treatment furnace according to the present invention has a temperature rising zone, a soaking zone, a slow cooling zone, and a cooling zone. In an atmosphere circulation type continuous heat treatment furnace having a plurality of unit zones forming an atmosphere circulation path by a ceiling fan and a furnace inner partition in a zone, a down flow system in which atmosphere circulation is jetted downward from a perforated plate, and A part of the circulating atmosphere flows into a predetermined unit zone into an adjacent unit zone on the side where the processing material is charged, so that a furnace gas flow from the last unit zone to the start unit zone is formed in the furnace. Further, a part of the circulation atmosphere may be caused to flow into the adjacent unit zone by providing a drift member at least in the hearth portion of the final unit zone. Furthermore, a part of the circulating atmosphere may be caused to flow into the adjacent unit zone side on the processing material charging side by providing a drift plate below the perforated plate of at least the final unit zone. By inclining the perforated plate, a part of the circulating atmosphere may be caused to flow into the adjacent unit zone side on the processing material charging side.

【0010】[0010]

【発明の実施の形態】つぎに、本発明の実施の形態につ
いて説明する。本発明を適用する雰囲気循環式連続熱処
理炉は、基本的には、前述した従来の構成のものと同一
であるため全体構成図は省略する。ただ、炉の所定の単
位帯域、たとえば、冷却帯40の最終単位帯域での循環
雰囲気の一部を処理材装入側の隣接単位帯域側に流入さ
せ、全体として炉気を最終単位帯域から始端単位帯域へ
流れるようにしたものである。そして、各単位帯域にお
いて処理材に吹き付けられる循環雰囲気の温度は、従来
同様、熱電対等で所定温度に制御されている。
Next, an embodiment of the present invention will be described. The atmosphere circulation type continuous heat treatment furnace to which the present invention is applied is basically the same as that of the above-described conventional structure, so that the overall configuration diagram is omitted. However, a part of the circulating atmosphere in a predetermined unit zone of the furnace, for example, in the last unit zone of the cooling zone 40 is caused to flow into the adjacent unit zone on the side where the processing material is charged, and the furnace gas is entirely moved from the last unit zone to the starting unit zone. It flows to the unit band. Then, the temperature of the circulating atmosphere blown to the processing material in each unit zone is controlled to a predetermined temperature by a thermocouple or the like as in the related art.

【0011】この偏流形成手段の第1の実施形態として
は、図1に示すように、単位帯域40cの前記天井ファ
ン4の真下に位置する炉底部に処理材装入側に対して傾
斜させた板状の偏流部材41を設置したものである。こ
の偏流部材41の設置により多孔板7から下方に吹き出
した雰囲気の一部は偏流部材41に衝突して装入側の隣
接する単位帯域40b側への流れを形成する。
As a first embodiment of this drift forming means, as shown in FIG. 1, the unit zone 40c is inclined at the furnace bottom located just below the ceiling fan 4 with respect to the processing material charging side. A plate-shaped drift member 41 is provided. A part of the atmosphere blown downward from the perforated plate 7 by the installation of the drift member 41 collides with the drift member 41 and forms a flow to the adjacent unit zone 40b on the charging side.

【0012】図2は第2の実施の形態を示し、多孔板7
の下部に回動可能な複数のガイド板からなる偏流部材4
1Aを設け、多孔板7から下方に吹き出す雰囲気の一部
を隣接する単位帯域40b側へ流れさせる。図3は図3
の実施の形態を示し、多孔板7自体を処理材抽出側を低
く、装入側を高くなるように傾斜させて多孔板7自体を
偏流部材41Bとして機能させたもので、図において、
多孔板7と炉底との距離は右側の方が左側より小さいた
め、多孔板7から雰囲気が吹き出すと、右側が左側に比
べて高圧となり、その結果、雰囲気は装入側単位帯域4
0b側へと流れることになる。
FIG. 2 shows a second embodiment, in which a perforated plate 7 is provided.
Drift member 4 comprising a plurality of guide plates rotatable below
1A is provided to allow a part of the atmosphere blown downward from the perforated plate 7 to flow toward the adjacent unit zone 40b. FIG. 3 shows FIG.
In this embodiment, the perforated plate 7 is inclined such that the processing material extraction side is low and the charging side is high so that the perforated plate 7 itself functions as the drift member 41B.
Since the distance between the perforated plate 7 and the furnace bottom is smaller on the right side than on the left side, when the atmosphere blows out from the perforated plate 7, the right side has a higher pressure than the left side.
It will flow to the 0b side.

【0013】なお、熱処理炉の長さ等により前記偏流部
材41,41A,41Bは他の単位帯域にも設置しても
よいことは勿論である。また、最小総必要熱量を得るた
めの炉気流量も、熱処理炉により異なるため適用熱処理
炉に対応する炉気流量とするものである。
It is a matter of course that the drift members 41, 41A and 41B may be installed in other unit zones depending on the length of the heat treatment furnace and the like. Further, the furnace air flow rate for obtaining the minimum total required heat amount also differs depending on the heat treatment furnace, so that the furnace air flow rate corresponding to the applicable heat treatment furnace is used.

【0014】[0014]

【発明の効果】以上の説明で明らかなように、本発明に
よれば、各単位帯域においてはそれぞれ所定温度の雰囲
気を処理材に吹きつけて処理材を熱処理する一方、炉内
雰囲気は最終単位帯域から始端単位帯域へと移動して、
つまり、処理材抽出側の雰囲気熱量を装入側へ移動させ
て熱収支を行なわせ、設備全体の燃料消費量を低減する
ことができるという効果を奏する。
As is apparent from the above description, according to the present invention, in each unit zone, an atmosphere at a predetermined temperature is blown to the processing material to heat-treat the processing material, while the atmosphere in the furnace is the final unit. Move from the band to the start unit band,
In other words, there is an effect that the amount of heat of the atmosphere on the processing material extraction side is moved to the charging side to perform the heat balance, and the fuel consumption of the entire facility can be reduced.

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

【図1】 本発明の操業方法を実施するための冷却帯の
断面図。
FIG. 1 is a cross-sectional view of a cooling zone for carrying out the operation method of the present invention.

【図2】 本発明の操業方法を実施するための他の実施
例を示す冷却帯の断面図。
FIG. 2 is a sectional view of a cooling zone showing another embodiment for carrying out the operation method of the present invention.

【図3】 本発明の操業方法を実施するための他の実施
例を示す冷却帯の断面図。
FIG. 3 is a sectional view of a cooling zone showing another embodiment for carrying out the operation method of the present invention.

【図4】 従来の雰囲気循環式連続熱処理炉の概略平面
図。
FIG. 4 is a schematic plan view of a conventional atmosphere circulation type continuous heat treatment furnace.

【図5】 図4の雰囲気循環式連続熱処理炉のヒートカ
ーブ。
FIG. 5 is a heat curve of the atmosphere circulation type continuous heat treatment furnace of FIG.

【図6】 図4の昇温帯、均熱帯の拡大断面図。FIG. 6 is an enlarged cross-sectional view of a warming zone and a tropical zone of FIG.

【図7】 図4の徐冷帯の拡大断面図。FIG. 7 is an enlarged sectional view of the slow cooling zone of FIG.

【図8】 図4の冷却帯の拡大断面図。FIG. 8 is an enlarged sectional view of the cooling zone of FIG. 4;

【図9】 図4のものにおける炉気流量と総必要熱量と
の関係を示すグラフ。
FIG. 9 is a graph showing the relationship between the furnace air flow rate and the total required heat amount in FIG.

【符号の説明】[Explanation of symbols]

1〜炉本体、2〜炉壁、3〜隔壁(バッフル)、4〜天
井ファン、5〜加熱手段、6〜循環路、7〜多孔板、1
0〜昇温帯、20〜均熱帯、30〜徐冷帯、40〜冷却
帯、10a,10b…,20a,20b…,30a,3
0b…,40a,40b…〜単位帯域、31〜給気ダク
ト、32〜排気ダクト、41,41A,41B〜偏流部
材、V〜コンベアチェーン。
1 furnace main body, 2 furnace wall, 3 partition wall (baffle), 4 ceiling fan, 5 heating means, 6 circulation circuit, 7 perforated plate, 1
0 to warming zone, 20 to soaking zone, 30 to slow cooling zone, 40 to cooling zone, 10a, 10b ..., 20a, 20b ..., 30a, 3
0b ..., 40a, 40b ... ~ unit band, 31 ~ air supply duct, 32 ~ exhaust duct, 41, 41A, 41B ~ drift member, V ~ conveyor chain.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 昇温帯、均熱帯、徐冷帯および冷却帯を
有するとともに、前記各帯に天井ファンと炉内隔壁とに
より雰囲気循環路を形成する複数の単位帯域を有する雰
囲気循環式連続熱処理炉において、雰囲気循環を多孔板
から下方に噴出させるダウンフロー方式とするととも
に、前記炉の所定単位帯域に循環雰囲気の一部を処理材
装入側の隣接単位帯域側に流入させて、炉内に最終単位
帯域から始端単位帯域への炉気流れを形成することを特
徴とする雰囲気循環式連続熱処理炉の操業方法。
An atmosphere circulation type continuous heat treatment having a temperature rising zone, a soaking zone, a slow cooling zone, and a cooling zone, and having a plurality of unit zones in each zone forming an atmosphere circulation path by a ceiling fan and a furnace inner partition. In the furnace, a down flow method in which the atmosphere circulation is ejected downward from the perforated plate, and a part of the circulating atmosphere is caused to flow into a predetermined unit zone of the furnace into an adjacent unit zone on the side where the processing material is charged, and the inside of the furnace is Forming a furnace gas flow from a final unit zone to a starting unit zone.
【請求項2】 少なくとも最終単位帯域の炉床部に偏流
部材を設けることにより循環雰囲気の一部を前記隣接単
位帯域側に流入させることを特徴とする前記請求項1に
記載の雰囲気循環式連続熱処理炉の操業方法。
2. The continuous atmosphere circulating system according to claim 1, wherein a part of the circulating atmosphere is caused to flow into the adjacent unit zone by providing a drift member at least in the hearth portion of the final unit zone. Operating method of heat treatment furnace.
【請求項3】 少なくとも最終単位帯域の多孔板下部に
偏流部材を設けることにより循環雰囲気の一部を処理材
装入側の隣接単位帯域側に流入させることを特徴とする
前記請求項1に記載の雰囲気循環式連続熱処理炉の操業
方法。
3. The method according to claim 1, wherein a part of the circulating atmosphere is caused to flow into the adjacent unit zone on the charging side of the processing material by providing a drift member at least below the perforated plate of the final unit zone. Operating method of continuous circulation heat treatment furnace of atmosphere circulation type.
【請求項4】 少なくとも最終単位帯域の多孔板を傾斜
させることにより循環雰囲気の一部を処理材装入側の隣
接単位帯域側に流入させることを特徴とする前記請求項
1に記載の雰囲気循環式連続熱処理炉の操業方法。
4. The atmosphere circulation according to claim 1, wherein at least a part of the circulation atmosphere is caused to flow into the adjacent unit zone on the side where the processing material is charged by inclining at least the perforated plate of the final unit zone. Operating method of continuous heat treatment furnace.
JP8310397A 1996-11-21 1996-11-21 Operating method of atmosphere circulation type continuous heat treatment furnace Expired - Fee Related JP2974629B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8310397A JP2974629B2 (en) 1996-11-21 1996-11-21 Operating method of atmosphere circulation type continuous heat treatment furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8310397A JP2974629B2 (en) 1996-11-21 1996-11-21 Operating method of atmosphere circulation type continuous heat treatment furnace

Publications (2)

Publication Number Publication Date
JPH10153387A true JPH10153387A (en) 1998-06-09
JP2974629B2 JP2974629B2 (en) 1999-11-10

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2308680A (en) * 1995-12-28 1997-07-02 Honda Motor Co Ltd Clamping workpieces before joining
JP2006500545A (en) * 2002-09-26 2006-01-05 ビーティーユー インターナショナル インコーポレイテッド Improvement of temperature distribution in convection heating furnace.
JP2008224192A (en) * 2007-03-15 2008-09-25 Koyo Thermo System Kk Continuous type kiln

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2308680A (en) * 1995-12-28 1997-07-02 Honda Motor Co Ltd Clamping workpieces before joining
GB2308680B (en) * 1995-12-28 1999-07-28 Honda Motor Co Ltd Method of combining workpieces
JP2006500545A (en) * 2002-09-26 2006-01-05 ビーティーユー インターナショナル インコーポレイテッド Improvement of temperature distribution in convection heating furnace.
US8328551B2 (en) 2002-09-26 2012-12-11 Btu International, Inc. Convection furnace thermal profile enhancement
JP2008224192A (en) * 2007-03-15 2008-09-25 Koyo Thermo System Kk Continuous type kiln

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