JPS59500063A - Preheating furnace for long materials - Google Patents

Preheating furnace for long materials

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Publication number
JPS59500063A
JPS59500063A JP83500472A JP50047283A JPS59500063A JP S59500063 A JPS59500063 A JP S59500063A JP 83500472 A JP83500472 A JP 83500472A JP 50047283 A JP50047283 A JP 50047283A JP S59500063 A JPS59500063 A JP S59500063A
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furnace
exhaust gas
preheating
tunnel
preheating furnace
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JPH0318112B2 (en
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エルハオス・フリ−ドリツヒ・ヴイルエルム
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エルハオス,フリ−ドリツヒ ヴイルエルム
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    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N27/00Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
    • G01N27/26Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating electrochemical variables; by using electrolysis or electrophoresis
    • G01N27/403Cells and electrode assemblies
    • G01N27/404Cells with anode, cathode and cell electrolyte on the same side of a permeable membrane which separates them from the sample fluid, e.g. Clark-type oxygen sensors
    • G01N27/4045Cells with anode, cathode and cell electrolyte on the same side of a permeable membrane which separates them from the sample fluid, e.g. Clark-type oxygen sensors for gases other than oxygen
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D9/00Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
    • C21D9/0075Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for rods of limited length
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/14Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment
    • F27B9/20Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment the charge moving in a substantially straight path
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N17/00Investigating resistance of materials to the weather, to corrosion, or to light
    • G01N17/02Electrochemical measuring systems for weathering, corrosion or corrosion-protection measurement

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Immunology (AREA)
  • Mechanical Engineering (AREA)
  • Pathology (AREA)
  • Analytical Chemistry (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Ecology (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Molecular Biology (AREA)
  • Environmental Sciences (AREA)
  • Electrochemistry (AREA)
  • Testing Resistance To Weather, Investigating Materials By Mechanical Methods (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Tunnel Furnaces (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Furnace Details (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Glanulating (AREA)
  • Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
  • Investigating And Analyzing Materials By Characteristic Methods (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 長尺材料の予熱炉 本発明は、長尺材料、例えば、バー、インゴット、ビレット及びその他の金属料 、特に、アルミニウム又はアルミニウム合金の長尺材料の予熱炉に関する。予熱 炉は、一体に結合され、又は個々に取外せるように結合された、特に薄肉の耐火 性炉殻によって構成された炉トンネルを有し、この炉トンネルは、バーナ及び高 温ガスノズル等の炉殻を貫通した加熱装置によって加熱されるように構成され、 加熱装置が、炉トンネルの長手方向に沿うようにこの炉トンネル内に搬入された 材料に向けられることにより、材料を直接加熱する。上記予熱炉は、また、予熱 炉の上部に配設された排ガスダクトを有する。[Detailed description of the invention] Preheating furnace for long materials The present invention applies to long materials such as bars, ingots, billets and other metal materials. In particular, it relates to a preheating furnace for elongated materials of aluminum or aluminum alloys. preheat Furnaces are made of particularly thin-walled refractory materials, which are joined together or individually removable. It has a furnace tunnel composed of a steel furnace shell, and this furnace tunnel has a burner and a high temperature furnace. configured to be heated by a heating device such as a hot gas nozzle that penetrates the furnace shell; The heating device was carried into this furnace tunnel along the longitudinal direction of the furnace tunnel. By being directed at the material, it heats the material directly. The above preheating furnace can also be used for preheating It has an exhaust gas duct located at the top of the furnace.

上述したような種類の公知の予熱炉(西ドイツ特許第1.807504号)にお いては、薄肉の炉殻が断熱材を使用せずに予熱炉の構造の一部として組込まれて いる。このため、特に、炉殻の外壁から熱放射によって熱が失われる。排ガスは 、炉トンネルの上部のスロットを通じて排ガスダクト内に吸引される。In the known preheating furnace of the type described above (West German Patent No. 1.807504) In some cases, a thin-walled furnace shell is incorporated as part of the preheating furnace structure without insulation. There is. Therefore, heat is lost through thermal radiation, particularly from the outer wall of the furnace shell. The exhaust gas is , is sucked into the exhaust gas duct through the slot at the top of the furnace tunnel.

炉トンネルから排ガスダクトに至る間において、熱が失われる。Heat is lost from the furnace tunnel to the exhaust gas duct.

このため、公知の予熱炉は、効率が低い。さらに、公知の予熱炉は、排ガスダク トが炉トンネルの上方において個別に設置されているから、複雑であるとともに 高価である。For this reason, known preheating furnaces have low efficiency. Furthermore, the known preheating furnace It is complicated and It's expensive.

本発明の目的は、本明細書の冒頭において明示したように、加熱のために供給さ れたエネルギが簡単で、かつ、小型の構造により従来よりも効率的に利用される 予熱炉を提供することである。The object of the invention, as specified at the beginning of the specification, is to energy can be used more efficiently than before due to its simple and compact structure The purpose is to provide a preheating furnace.

上記の目的に対処するために、本発明は、本明細書の冒頭において明示した予熱 炉において、炉トンネルが断熱材で覆われた排ガスダクトに組込まれている。排 ガスダクトの断熱材は、炉トンネルの新穀を少な(ともその中央部分において外 側から覆うことが望ましい。そうすれば、炉殻の下部は、炉殻の組立及び保守の いずれにも煩しさがない。In order to address the above objects, the present invention provides a preheating method as specified at the beginning of the specification. In the furnace, the furnace tunnel is integrated into the exhaust gas duct covered with insulation. Exclusion The insulation of the gas ducts is suitable for keeping the new grain in the furnace tunnel small (at least in its central part It is desirable to cover from the sides. That way, the lower part of the furnace shell can be used for assembly and maintenance of the furnace shell. There is no hassle in either.

本発明によれば、エネルギは、極めて良好に利用される。この理由は、排ガスが 炉トンネルから、例えば、立てて配設された複数個の炉殻間の上部の隙間を通じ て、熱量を失うことなく排ガスダクトに移送されるからである。本発明の利点と して、炉トンネルの上部中央は、排ガスダクトのみによって、すなわち、その他 の手段を一切用いることなしに、断熱されている。According to the invention, energy is utilized very well. The reason for this is that exhaust gas From the furnace tunnel, for example, through the upper gap between multiple furnace shells arranged vertically. This is because the heat is transferred to the exhaust gas duct without losing heat. Advantages of the invention and so that the upper center of the furnace tunnel is separated only by the exhaust gas duct, i.e. insulation without using any means.

炉トンネルの下部の断熱は、組立作業及び保守をし易くするために、行われてい ない。本発明は、炉殻の下部から熱放射によって失われる熱量は、比較的小さい ことを見出した。上述のように、炉殻の下部から断熱材を取去ると、例えば、バ ーナ、炉殻の支持フレーム、及び材料を予熱するためのコンベアから成る集合体 を受入れ、かつ、集合体に触れるための空間が残されることになるので、利点が 多い。The lower part of the furnace tunnel is insulated to facilitate assembly and maintenance. do not have. In the present invention, the amount of heat lost by thermal radiation from the lower part of the furnace shell is relatively small. I discovered that. As mentioned above, removing insulation from the bottom of the furnace shell can cause e.g. assembly consisting of a furnace, support frame for the furnace shell, and a conveyor for preheating the material This has the advantage that there is space left to accept and interact with the aggregate. many.

上記断熱材は、支持フレームから上向きに突出していてもよいし、また、炉殻の 上部に適合するように形成されていてもよい。The insulation material may protrude upwardly from the support frame or may be attached to the furnace shell. It may be shaped to fit on top.

本発明の一態様においては、特に組立及び分解が容易であり、この態様は、断熱 材が、予熱炉の支持フレームに固定された支持部材によって支持され、この支持 部材の上方に配設された取外し自在の上部断熱部材を有する一方、断熱材の下部 断熱部材が炉殻を横から支持するとともにこれら炉殻を断熱するへことを特徴と する。One aspect of the invention is particularly easy to assemble and disassemble; The material is supported by a support member fixed to the support frame of the preheating furnace, and this support having a removable upper insulation member disposed above the member, while a lower part of the insulation The heat insulating member supports the furnace shell from the side and also insulates the furnace shell. do.

本発明の好適な一態様によれば、炉トンネルの周囲に下部及び上部バーナ列が設 けられているとともに、上部バーナ列は、取外し自在の断熱部材を貫通しており 、また、下部バーナ列は、断熱されていない、炉殻の下部に設けられている。し がして、バーナが貫通した各断熱部材は、炉殻を構成し、かつ、この断熱部材と 対向するブロックと同一長さである。According to a preferred embodiment of the invention, lower and upper burner rows are provided around the furnace tunnel. The upper burner row passes through a removable insulation member. , and the lower burner row is located in the lower part of the furnace shell, which is not insulated. death Each insulating member through which the burner penetrates constitutes the furnace shell, and is connected to this insulating member. It has the same length as the opposing block.

下部バーナ列のみが必要な場合には、これらのバーナは、断熱材よりも下方にお いて、炉トンネルの内部に開口し、排ガスダクトは、取外し自在な一体構造物と なる。このように予熱炉が構成されている場合は、炉殻の全体又は一部の交換を 容易にするため排ガスダクトを一体として取外すことができるので、特に、炉殻 の組立、保守又は交換が簡単となる。If only the bottom burner row is required, these burners should be placed below the insulation. The exhaust gas duct opens into the inside of the furnace tunnel, and the exhaust gas duct is a removable integral structure. Become. If the preheating furnace is configured in this way, it is recommended to replace all or part of the furnace shell. The exhaust gas duct can be removed as a whole for ease of use, especially in the furnace shell. assembly, maintenance or replacement becomes easy.

これまで説明して来たような種類の最新型予熱炉においては、高温排ガスは、排 ガスダクトを通過して材料を予熱するための予熱炉又は他の炉の予熱ゾーンに導 入される(西ドイツ特許出願公開第2.637.646号)から、特に燃料の経 済的利用が保証されている。これら最新型予熱炉においても、特に、予熱炉の排 ガスが上流の予熱炉を加熱するのに役立つ種類のものは利点が多い。上流の予熱 炉は、少なくとも1個のファンを通じて、予熱すべき材料に沿って配置された少 なくとも1列のスロット型ノズルまで排ガスを移送し、この排ガスを材料に吹付 けるように構成されているものである。In modern preheating furnaces of the type described so far, the high-temperature exhaust gas is Pass through a gas duct to the preheating zone of a preheating furnace or other furnace for preheating the material. (West German Patent Application No. 2.637.646). Economical use is guaranteed. Even in these latest types of preheating furnaces, in particular, There are many advantages to the type in which the gas serves to heat the upstream preheating furnace. Upstream preheating The furnace operates through at least one fan and a small fan placed along the material to be preheated. Transport the exhaust gas to at least one row of slotted nozzles and spray this exhaust gas onto the material. It is constructed so that it can be used.

本発明によれば、予熱炉の炉内が幾つかの加熱制御ゾーンに分割され、これらの 加熱制御ゾーンが共通の排ガスダクトを通じて連通している場合に、特に利点が 多い。定格化された温度に応じてそれぞれの加熱制御ゾーンが閉じられる場合に は、排ガスダクトによって連通していても、−の加熱制御ゾーンは、他の加熱制 御ゾーンの影響を受けない。導かれたガスは、すべて、共通の排ガスダクトの上 部を長手方向に通過した後、予熱ゾーンに移送されるか、又は材料を予熱するた めに、燃料の熱容量を完全に利用するための上流の予熱炉に上述したような方法 で移送されることが望ましい。上述した上流の予熱炉は、下流の炉に連続する予 熱炉及びこの予熱炉よりも上流にある、複数基の予熱炉から成る灯群の一部とし て位置づけられるものである。According to the present invention, the inside of the preheating furnace is divided into several heating control zones, and these This is particularly advantageous if the heating control zones communicate through a common exhaust gas duct. many. When the respective heating control zone is closed according to the rated temperature The - heating control zone is connected to other heating control zones even if they are connected by an exhaust gas duct. Not affected by the control zone. All guided gases are routed over a common exhaust gas duct. After passing through the section longitudinally, it is transferred to a preheating zone or used to preheat the material. In order to fully utilize the heat capacity of the fuel, an upstream preheating furnace can be used as described above. It is desirable to transport the The upstream preheating furnace described above has a preheating furnace connected to the downstream furnace. As part of a lamp group consisting of a thermal furnace and multiple preheating furnaces upstream of this preheating furnace. It is positioned as such.

本発明の好適な実施例を、実施された2基の予熱炉の横断面図に基づいて、さら に詳しく説明する。A preferred embodiment of the present invention will be further described based on cross-sectional views of two preheating furnaces implemented. will be explained in detail.

図面中、 第1図は、本発明による予熱炉の瞥1実施例に2いて、第3図のI−I線に母う 横断面図である。In the drawing, FIG. 1 shows a first embodiment of a preheating furnace according to the present invention, and the line I--I in FIG. FIG.

第2図は、第2実施例において同一箇所の横断面図である。FIG. 2 is a cross-sectional view of the same location in the second embodiment.

第3図は、本発明の変形例による、予熱炉及び上流加熱炉から構成された灯群の 一部断面側面図である。FIG. 3 shows a lamp group consisting of a preheating furnace and an upstream heating furnace according to a modification of the present invention. FIG. 3 is a partially sectional side view.

第4図は、第1図又は第2図に示された予熱炉な有する、上流に結合された灯群 の加熱炉において、第3図のIV−IV線断面図である。FIG. 4 shows a group of lights connected upstream having the preheating furnace shown in FIG. 1 or 2. FIG. 4 is a sectional view taken along the line IV-IV in FIG. 3 in the heating furnace.

図示された予熱炉は、鋼製の支持フレーム10を有する。The illustrated preheating furnace has a support frame 10 made of steel.

予熱炉の下部空間に、二重走行コンベアチェーン13が設げられており、この二 重走行コンベアチェーン13に、バー又はビレットのような勢料−−J犯を運ぶ キャリア12が増付けられている。上記二重走行コンベアチェーン1゜3は、複 数個の半円筒状炉殻14によって構成された円筒状炉トンネル15内で材料を間 欠的に押し進める。炉殻14は、それらの下部において、キャリアレール16上 に枢動自在に支持され、上部において、スペーサ17により定位置に保持されて いる。A double running conveyor chain 13 is installed in the lower space of the preheating furnace. A heavy conveyor chain 13 conveys a force such as a bar or billet--J. A carrier 12 is added. The above double running conveyor chain 1゜3 is a double running conveyor chain. The material is separated in a cylindrical furnace tunnel 15 made up of several semi-cylindrical furnace shells 14. Push forward intermittently. In their lower part, the furnace shells 14 are mounted on carrier rails 16. It is pivotably supported by a There is.

第1図に示されている実施例においては、図面に対して垂直となる炉の長手方向 に配設された、複数本の予混合バーナ18から成るーのバーナ列が一列を成す炉 殻14に対して設けられている。バーナ18は、バーナノズル20を有し、この バーナノズル20は、炉殻14に形成された開口21を通じて円筒状炉トンネル 15内に突出し、材料に直接作用する。バーナ18は、径が異なる材料」を予熱 する時、材料表面が熱伝達のためにうまく利用され、かつ、温度勾配が材料1の 横断面にお〜・て回転対称となるように、配置されている。バーナノズル2oは 、所望の温度勾配が得られるように調整される。In the embodiment shown in Figure 1, the longitudinal direction of the furnace is perpendicular to the drawing. A furnace in which a burner row consisting of a plurality of premix burners 18 is arranged in a row. Provided for the shell 14. The burner 18 has a burner nozzle 20, which The burner nozzle 20 is inserted into a cylindrical furnace tunnel through an opening 21 formed in the furnace shell 14. 15 and acts directly on the material. The burner 18 preheats materials with different diameters. When the material surface is well utilized for heat transfer and the temperature gradient is They are arranged so as to be rotationally symmetrical in the cross section. burner nozzle 2o , adjusted to obtain the desired temperature gradient.

バーナ18の代りに、材料1に直接作用する熱ガスノズルを使用してもよい。ま た、熱ガスとしては、公知の電気的手段によって加熱されたエアを使用すること ができる。Instead of the burner 18, a hot gas nozzle acting directly on the material 1 may also be used. Ma In addition, air heated by known electrical means may be used as the hot gas. Can be done.

排ガスは、炉トンネル15から立上り、スペーサ17の取付部において左右の炉 殻14が形成する長手方向のスロッ)30を通り、垂直路を直接抜けて排ガスダ クト32に至る。この排ガスダクト32から、排ガスは、材料1のための予熱部 (図示せず)に送られ、例えば、ファン(図示せず)によって吸引されることに より予熱炉よりも上流に滞留される。排ガスダクト32は、断熱材を有する。こ の断熱材のうち下部断熱部材54が予熱炉の全長に亘って延設されている。これ ら下部断熱部材54は、炉トンネル15が配設されるためのギャップを残して配 設されるとともに、外側から炉殻14の中央部分に当接している。下部断熱部材 54は、キャリアビーム52に支持されており、これらキャリアビーム52は、 支持フレームlo上に固定されている。排ガスダクト3,2の主要部は、2本の 垂直断熱部材56により区切られている。しかして、断熱材の上部断熱部材58 は、垂直断熱部材56と一体である。Exhaust gas rises from the furnace tunnel 15 and passes through the left and right furnaces at the attachment point of the spacer 17. The exhaust gas pipe passes through the longitudinal slot (30) formed by the shell 14 and passes directly through the vertical passage. This leads to section 32. From this exhaust gas duct 32, the exhaust gas flows into the preheating section for the material 1. (not shown) and, for example, to be sucked by a fan (not shown). It is retained upstream of the preheating furnace. The exhaust gas duct 32 has a heat insulating material. child Among the heat insulating materials, a lower heat insulating member 54 extends over the entire length of the preheating furnace. this The lower heat insulating member 54 is disposed leaving a gap for the furnace tunnel 15 to be disposed. At the same time, it is in contact with the central portion of the furnace shell 14 from the outside. Lower insulation member 54 are supported by carrier beams 52, and these carrier beams 52 are It is fixed on a support frame lo. The main parts of the exhaust gas ducts 3 and 2 are composed of two It is separated by a vertical insulation member 56. Therefore, the upper insulation member 58 of the insulation material is integral with the vertical insulation member 56.

第1図の実施例においては、垂直断熱部材56も、上部断熱部材58も予熱炉の 全長に亘って延設されている。したがって、これら垂直断熱部材56及び上部断 熱部材58は、一体として取外すことができる。炉殻14は、下部断熱部材54 によって横の方から保持されている。しかし、スペーサ17が取外されることに よって、炉殻14は、キャリアレール16に設けられたそれぞれの支点に対し容 易に内方に回動させることができ、交換のために別々に取外すことができる。In the embodiment of FIG. 1, both the vertical insulation member 56 and the upper insulation member 58 are connected to the preheating furnace. It extends the entire length. Therefore, these vertical insulation members 56 and the upper section Thermal member 58 can be removed as a unit. The furnace shell 14 has a lower insulation member 54 It is held from the side by However, spacer 17 was removed. Therefore, the furnace shell 14 has a capacity relative to each fulcrum provided on the carrier rail 16. It can be easily pivoted inward and removed separately for replacement.

上記断熱材は、例えば2層の断熱材から成る。内層は、断熱効果が良好であるが 、蓄熱効果が不良のセラミック繊維から成るものであり、他方、外層は、低温域 に置かれるから、鉱物繊維によって作られている。The above-mentioned heat insulating material is composed of, for example, two layers of heat insulating material. The inner layer has good insulation effect, but , is made of ceramic fiber with poor heat storage effect, while the outer layer is made of ceramic fiber with poor heat storage effect. It is made from mineral fibers.

第2図に示された実施例は、下側に配設されたバーナ18の列の他に上側におい て−の炉殻14の列に対し一列のバーナ19を配設した点においてのみ、第1図 の実施例と相違する。絞り弁24が燃料供給ライン23に設けられており、この 絞り弁24によって下側のバーナ18を基準として上側のバーナ19が調整され る。In addition to the row of burners 18 arranged on the lower side, the embodiment shown in FIG. Only in the point that one row of burners 19 is arranged for each row of furnace shells 14, as shown in FIG. This is different from the embodiment. A throttle valve 24 is provided in the fuel supply line 23, and this The upper burner 19 is adjusted with the lower burner 18 as a reference by the throttle valve 24. Ru.

追加された上側のバーナ190列に対しては、・下部断熱部材54と排ガスダク ト32の主要部との間に垂直断熱部材59を位置決めすることを要する。垂直断 熱部材59は、炉殻14と対応して複数個の部分に分割されている。下部断熱部 材54は、予熱炉の全長に亘って延設されている。排ガスダクト32の主要部は 、断熱部材60.62及び64を有し、これらの断熱部材60.62及び64は 、一体に結合されており、したがって一体として取外すことができる。炉殻14 を交換するためには、断熱部材60.62及び64を持ち上げなければならない 。しかして、第1図の実施例の場合と同様に、スペーサ17を取外すことによっ て対になった炉殻14を交換し得るように、交換する側の炉殻14に対応する断 熱部材59を取外さなければならない。第2図に示された実施例は、第1図に示 された実施例に比べて若干複雑な構成を有しているが、これは、材料1をより均 一に加熱するためにはやむをえない。For the added 190 rows of upper burners, the lower insulation member 54 and the exhaust gas duct It is necessary to position the vertical heat insulating member 59 between the main part of the seat 32 and the main part of the seat 32. Vertical section The heating member 59 is divided into a plurality of parts corresponding to the furnace shell 14. Lower insulation part The material 54 extends over the entire length of the preheating furnace. The main parts of the exhaust gas duct 32 are , has insulating members 60, 62 and 64, and these insulating members 60, 62 and 64 have , are joined together and can therefore be removed as one piece. Furnace shell 14 In order to replace the insulation elements 60, 62 and 64 must be lifted. . Therefore, as in the case of the embodiment shown in FIG. In order to be able to exchange the paired furnace shells 14 by Thermal member 59 must be removed. The embodiment shown in FIG. Although it has a slightly more complicated configuration than the example described above, this makes material 1 more uniform. It is unavoidable in order to heat it all at once.

第3図の右半部90は、第1図又は第2図に示された予熱炉の側面を示しており 、第3図の左半部は、予熱炉から排出される排ガスによって加熱される上流の予 熱炉を示している。上流の予熱炉を加熱するために、排ガスダクト32は、その 開口部33によって上流の予熱炉40の右端面34において開口している(第3 図参照)。上流の予熱炉40の詳細は、第4図に示されている。開口部33を介 して排ガスダクト32に連通し、予熱炉90の断熱材と同様の断熱材42によっ て保護された炉内41に、前後に並んだ複数個の循環ゾーン、例えば、2個の循 環ゾーン47及び48が設けられている。各循環ゾーン47又は48は、排ガス ダクト32から、第3図中、矢印F方向へ排ガスを吸引し、2列のスロット型ノ ズル44を通じて材料に吹付ける。ノズル44は、材料に向って収束するように 両側に設けられている。材料1は、二重走行コンベアチェーン13によって、各 循環ゾーン47又は48の処理室45の内部を運搬方向Tに送られる。上記二重 走行コンベアチェーン13は、予熱炉40及び90のいずれをも通過する。材料 1が運搬方向Tに送られた後、排ガスは、ファン43によつ【処理室45から吸 引し尽され、再度、循環されるか又は吐出管46を通じて放出される。The right half 90 of FIG. 3 shows the side surface of the preheating furnace shown in FIG. 1 or 2. , the left half of Figure 3 shows the upstream preheater heated by the exhaust gas discharged from the preheating furnace. Shows a thermal furnace. To heat the upstream preheating furnace, the exhaust gas duct 32 The opening 33 opens at the right end surface 34 of the upstream preheating furnace 40 (the third (see figure). Details of the upstream preheating furnace 40 are shown in FIG. Through the opening 33 is connected to the exhaust gas duct 32 and is provided with a heat insulating material 42 similar to the heat insulating material of the preheating furnace 90. Inside the furnace 41, which is protected by Annular zones 47 and 48 are provided. Each circulation zone 47 or 48 has exhaust gas Exhaust gas is sucked from the duct 32 in the direction of arrow F in Fig. 3, and two rows of slot-shaped The material is sprayed through the nozzle 44. The nozzle 44 is configured to converge toward the material. Located on both sides. The material 1 is transported by a double running conveyor chain 13 to each It is sent in the transport direction T inside the processing chamber 45 in the circulation zone 47 or 48. Double above Traveling conveyor chain 13 passes through both preheating furnaces 40 and 90. material 1 is sent in the transport direction T, the exhaust gas is sucked from the processing chamber 45 by the fan 43. It is exhausted and recycled again or discharged through the discharge pipe 46.

第3図において右から左へ連続する、循環ゾーン47及び48においては、運搬 方向Tと反対方向に漸低する温度勾配が確立される。各循環ゾーンにおいて温度 制御が可能なように材料が挿入されるのは、このように排ガス多段案内にも似た システムのためである。したがって、排ガスの熱容量は、最適状態で利用されて いる。このように、第3図及び第4図に示した予熱炉は、特に、経済的、すなわ ち、特に低熱費であるという特徴を有する。In circulation zones 47 and 48, which are continuous from right to left in FIG. A gradually decreasing temperature gradient in the opposite direction to direction T is established. Temperature in each circulation zone The material is inserted in such a way that it can be controlled, similar to this multi-stage exhaust gas guide. It's for the system. Therefore, the heat capacity of the exhaust gas is optimally utilized. There is. Thus, the preheating furnace shown in FIGS. 3 and 4 is particularly economical, i.e. In particular, it is characterized by low heating costs.

IG 1IG 1

Claims (1)

【特許請求の範囲】 1.長尺材料、例えば、バー、インゴット、ビレット及びその他の金属材、特に アルミニウム又はアルミニウム合金の長尺材料の予熱炉であって、この予熱炉が 、一体に結合され、又は個々に取外せるように結合された、特に薄肉の耐火性炉 殻によって構成された炉トンネルを有し、この炉トンネルがバーナ及び高温ガス ノズル等のような、炉殻を貫通した加熱装置によって加熱されるように構成され 、加熱装置が、炉トンネルの長手方向に沿うようにこの炉トンネル内に搬入され た材料に向けられることにより、材料を直接加熱するとともに、上記予熱炉がさ らにこの予熱炉の上部に配設された排ガスダクトを頁するものにおいて、上記炉 トンネル(15)は、断熱材を有する排ガスダク)(32)内に組込まれたこと を特徴とする予熱炉。 2 請求の範囲第1項に記載の予熱炉であって、上記排ガスダク)(32)の断 熱材が少なくとも炉トンネル(15)の中央部分の外側からこの炉トンネル(1 5)の複数個の炉殻(14)を覆うことを特徴とするもの。 3、請求の範囲第1項又は第2項に記載の予熱炉であって、上記断熱材が、予熱 炉の支持フレーム(10)上に固定された支持部材(52)によって支持され、 かつ、この支持部材(52)の上方に配設された取外し自在の断熱部材(54, 56及び58;59,60.62及び64)を有し、断熱材の下部断熱部材(5 4)が炉殻(14)を横から支持し、かつ、断熱することを特徴とするもの。 4、請求の範囲第3項に記載の予熱炉であって、上記支持部材(52)上に載置 された複数個の下部断熱部材(54)が、排ガスダクトを構成する他の断熱部分 (56及び58;59,60.62及び64)から個々に取外し自在に構成され たことな特徴とするもの。 五 下部及び上部バーナ列が設けられ、炉トンネルの周囲に配置された請求の範 囲第3項又は第4項に記載の予熱炉であって、上部バーナ列のバーナ(19)が 域外し自在の断熱部材(59)を貫通し、下部バーナ列のバーナ(18)が、断 熱されていない、炉殻の下部に設けられるとともに、バーナ(19)が貫通する 各断熱部材(59)は、全炉殻のうちの対応する炉殻と同一の長さを有すること を特徴とするもの。 6、請求の範囲第1項ないし第4項に記載の予熱炉であって、全列のバーナが断 熱材の下方において、炉トンネル(15)内に開口するとともに、排ガスダクト (32)が一体として取外し自在に構成されたことを特徴とするもの。 7、請求の範囲第1項ないし第5項のうちの1項に記載の予熱炉であって、上記 断熱材が少なくとも一重のセラミック繊維内層と、少なくとも一重の鉱物繊維外 層とを含むことを%徴とするもの。 a 材料に沿って配設され、この材料に排ガスを吹付ける、少なくとも1列のス ロット型ノズルに、少なくとも1個のファンを通じて排ガスを移送する上流の予 熱炉を、請求の範囲第1項ないし第7項に記載の予熱炉の排ガスが加熱する灯群 であって、上記排ガスダク)(32)が予熱炉(40)の炉内(41)にほぼ整 列して配置され、炉内にはファン(43)が設けられるとともに炉内が断熱材( 42)によって同様に保護され、さらに、上記排ガスダク)(32)がその前端 (33)において、炉内(41)に開口したことを特徴とするもの。[Claims] 1. Long materials, such as bars, ingots, billets and other metal materials, especially A preheating furnace for long materials of aluminum or aluminum alloy, the preheating furnace being , particularly thin-walled refractory furnaces, joined together or individually removable It has a furnace tunnel composed of a shell, and this furnace tunnel is used for the burner and high-temperature gas. configured to be heated by a heating device that penetrates the furnace shell, such as a nozzle, etc. , the heating device is carried into this furnace tunnel along the longitudinal direction of the furnace tunnel. The preheating furnace heats the material directly and heats the material directly. Furthermore, in the case where the exhaust gas duct is installed in the upper part of the preheating furnace, The tunnel (15) is incorporated into the exhaust gas duct (32) having insulation material. A preheating furnace featuring: 2. The preheating furnace according to claim 1, wherein the exhaust gas duct) (32) is disconnected. The heating material flows from at least the outside of the central part of the furnace tunnel (15) into the furnace tunnel (15). 5), which is characterized by covering a plurality of furnace shells (14). 3. The preheating furnace according to claim 1 or 2, wherein the heat insulating material is supported by a support member (52) fixed on the support frame (10) of the furnace; In addition, a removable heat insulating member (54, 56 and 58; 59, 60. 62 and 64), and the lower insulation member (5 4) is characterized in that it laterally supports the furnace shell (14) and insulates it. 4. The preheating furnace according to claim 3, which is placed on the support member (52). The plurality of lower heat insulating members (54) are connected to other heat insulating parts forming the exhaust gas duct. (56 and 58; 59, 60. 62 and 64) can be individually removed. What makes it unique? 5. Claims provided with lower and upper burner rows and arranged around the furnace tunnel. 4. The preheating furnace according to item 3 or 4, wherein the burner (19) in the upper burner row is The burners (18) of the lower burner row penetrate the removable heat insulating member (59) and It is installed in the lower part of the furnace shell, which is not heated, and the burner (19) passes through it. Each heat insulating member (59) has the same length as the corresponding furnace shell among all the furnace shells. characterized by. 6. The preheating furnace according to claims 1 to 4, wherein all rows of burners are disconnected. Below the heating material, it opens into the furnace tunnel (15) and an exhaust gas duct. (32) is constructed as one unit and can be freely removed. 7. A preheating furnace according to one of claims 1 to 5, which comprises: The insulation consists of at least one inner layer of ceramic fibers and at least one outer layer of mineral fibers. % indicates that it contains layers. a. At least one row of strips arranged along the material and blowing exhaust gas onto the material. The rotary nozzle has an upstream pre-stage for transporting the exhaust gas through at least one fan. A group of lamps in which a thermal furnace is heated by the exhaust gas of the preheating furnace according to claims 1 to 7. The exhaust gas duct) (32) is located in the furnace (41) of the preheating furnace (40) in a substantially uniform manner. They are arranged in rows, and a fan (43) is provided inside the furnace, and the inside of the furnace is covered with a heat insulating material ( 42), and furthermore, the exhaust gas duct) (32) is located at its front end (33), characterized in that it opens into the furnace interior (41).
JP83500472A 1982-02-02 1983-02-01 Preheating furnace for long materials Granted JPS59500063A (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
DE32034334SE 1982-02-02
DK86482 1982-02-26
DK126082 1982-03-19
PCT/DK1983/000022 WO1983003007A1 (en) 1982-02-26 1983-02-25 Method and device for determining hydrogen flux

Publications (2)

Publication Number Publication Date
JPS59500063A true JPS59500063A (en) 1984-01-12
JPH0318112B2 JPH0318112B2 (en) 1991-03-11

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JP58500846A Pending JPS59500331A (en) 1982-02-26 1983-02-25 Method and device for measuring hydrogen flow

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EP (1) EP0103588A1 (en)
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AU (1) AU1331083A (en)
DK (1) DK492183A (en)
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WO (1) WO1983003007A1 (en)

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BR9501061A (en) * 1995-03-14 1997-05-06 Petroleo Brasileiro Sa Electrochemical sensor and process for measuring hydrogen permeation
US6894884B2 (en) 1997-04-08 2005-05-17 Xzy Attenuators, Llc Offset pathway arrangements for energy conditioning
US6018448A (en) 1997-04-08 2000-01-25 X2Y Attenuators, L.L.C. Paired multi-layered dielectric independent passive component architecture resulting in differential and common mode filtering with surge protection in one integrated package
US6554981B2 (en) * 1998-09-14 2003-04-29 Saudi Arabian Oil Company Hydrogen permeation probe
PL394698A1 (en) * 2011-04-29 2012-11-05 Instytut Chemii Fizycznej Polskiej Akademii Nauk Probe for determining the penetration rate of hydrogen into metal and a device comprising such a probe
CN102323205B (en) * 2011-05-11 2015-03-18 中国科学院海洋研究所 Method for detecting hydrogen permeation current and hydrogen distribution at metal stress corrosion crack
EP3280986B1 (en) 2015-04-07 2020-05-13 University of New Brunswick System and method for monitoring hydrogen flux
ES2573178B2 (en) * 2015-09-18 2017-07-31 Universidad Complutense De Madrid Sensor for corrosion monitoring through electrochemical impedance and noise measurements and polarization resistance and use thereof
EP4060322A1 (en) * 2021-03-16 2022-09-21 Polski Koncern Naftowy Orlen S.A. Probe for corrosion rate measurement

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US2948237A (en) * 1958-02-17 1960-08-09 Florian C Toepel Revolving hearth for a combustion chamber
NL302879A (en) * 1963-02-25
US3410780A (en) * 1965-10-22 1968-11-12 United Nuclear Corp Electrochemical hydrogen meter
US3629090A (en) * 1968-09-09 1971-12-21 North American Rockwell Apparatus for measuring hydrogen absorption
US3772178A (en) * 1968-10-03 1973-11-13 Petrolite Corp Electrode for corrosion test
JPS51115212A (en) * 1975-04-02 1976-10-09 Daido Steel Co Ltd Apparatus for heat treatment with non-oxidizing atmosphere
US4065373A (en) * 1976-04-26 1977-12-27 Petrolite Corporation Hydrogen patch cell
DE2637646B2 (en) * 1976-08-20 1978-08-10 Friedrich Wilhelm Dipl.- Ing. 5600 Wuppertal Elhaus Heating furnace
GB1585070A (en) * 1977-11-22 1981-02-25 Nat Res Dev Electrochemical cell
US4221651A (en) * 1979-06-25 1980-09-09 Rockwell International Corporation Electrochemical cell for measuring hydrogen in metal

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EP0103588A1 (en) 1984-03-28
DK492183D0 (en) 1983-10-26
AU1331083A (en) 1983-09-08
JPS59500331A (en) 1984-03-01
JPH0318112B2 (en) 1991-03-11
DK492183A (en) 1983-10-26
WO1983003007A1 (en) 1983-09-01

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