JPH0116763Y2 - - Google Patents

Info

Publication number
JPH0116763Y2
JPH0116763Y2 JP7359082U JP7359082U JPH0116763Y2 JP H0116763 Y2 JPH0116763 Y2 JP H0116763Y2 JP 7359082 U JP7359082 U JP 7359082U JP 7359082 U JP7359082 U JP 7359082U JP H0116763 Y2 JPH0116763 Y2 JP H0116763Y2
Authority
JP
Japan
Prior art keywords
plates
hearth
ceiling
gas
preheating zone
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
JP7359082U
Other languages
Japanese (ja)
Other versions
JPS58176957U (en
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 filed Critical
Priority to JP7359082U priority Critical patent/JPS58176957U/en
Publication of JPS58176957U publication Critical patent/JPS58176957U/en
Application granted granted Critical
Publication of JPH0116763Y2 publication Critical patent/JPH0116763Y2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Furnace Details (AREA)

Description

【考案の詳細な説明】 本考案は、バーナを設けない予熱帯を有する鋼
片材料などの加熱炉に関するものである。
[Detailed Description of the Invention] The present invention relates to a heating furnace for steel billet materials, etc., which has a preheating zone without a burner.

従来の金属加熱炉では、たとえば、第1図およ
び第2図に示すように、加熱炉a内のスラブb
は、仕切壁jで区画された予熱帯d、加熱帯e、
均熱帯fを矢印iで示すように移動しながら、
900〜1200℃に加熱される。前記加熱帯eと均熱
帯fには、天井バーナgとサイドバーナhを有す
るが、予熱帯dにはバーナがなく、加熱帯eから
流れてくる800〜1000℃の高温排ガスでスラブサ
ポートc上のスラブbを予熱する。すなわち、従
来の予熱帯dは、第1図のごとくであり、ガス流
kは流れ易い所のみを通つて流れるため、予熱帯
dの高さ方向にガスの滞溜およびドラフトによる
大きな温度成層を生じ、有効ガスふく射径が小さ
く、さらに天井および炉床温度がガス温度より低
下することから伝熱量の有効率が低かつた。また
予熱帯d内の断面が一様で広いため、ガス流速は
秒速0.5メートル程度と低く、対流伝熱量は小さ
かつた。これに対し、予熱帯dの伝熱効率の向上
として、排ガスをフアンによりスラブに噴付ける
噴流予熱帯があるが、この場合、フアンの動力の
増大、設備費の増加、とくにホツトチヤージスラ
ブでは、フアンの耐熱性が500℃位までと低く、
使用できない等の問題を生じていた。また対流伝
熱増加のために、予熱帯dの高さHを低くする
と、ガス層厚さが低下し、ふく射伝熱量が低下し
た。
In a conventional metal heating furnace, for example, as shown in FIGS. 1 and 2, a slab b in a heating furnace a is
are a preheating zone d, a heating zone e, and a heating zone e divided by a partition wall j.
While moving through the soaking zone f as indicated by arrow i,
Heated to 900-1200℃. The heating zone e and the soaking zone f have a ceiling burner g and a side burner h, but there is no burner in the preheating zone d, and the high temperature exhaust gas of 800 to 1000 degrees Celsius flowing from the heating zone e burns the top of the slab support c. Preheat slab b. In other words, the conventional preheating zone d is as shown in Fig. 1, and since the gas flow k flows only through easy-to-flow areas, large temperature stratification due to gas accumulation and draft occurs in the height direction of the preheating zone d. The effective gas radiation diameter was small, and the ceiling and hearth temperatures were lower than the gas temperature, so the effective rate of heat transfer was low. In addition, because the cross section within the preheating zone d was uniform and wide, the gas flow velocity was low at about 0.5 meters per second, and the amount of convective heat transfer was small. On the other hand, in order to improve the heat transfer efficiency of the preheating zone d, there is a jet preheating zone in which the exhaust gas is jetted onto the slab by a fan, but in this case, the power of the fan increases and the equipment cost increases, especially in hot charge slabs. The heat resistance of the fan is low, up to about 500℃.
This caused problems such as unusability. Furthermore, when the height H of the preheating zone d was lowered to increase convective heat transfer, the gas layer thickness decreased and the amount of radiation heat transfer decreased.

本考案は、バツフル板を交互に設けることによ
り、フアンによらないで、ガスの滞溜がなく、よ
く混合されて高温となり、ふく射伝熱量の増加を
図ることができる予熱帯を提供することを目的と
するものである。
The present invention provides a preheating zone that does not require a fan, does not require a fan, and can mix well and reach a high temperature by providing alternating buttful plates, thereby increasing the amount of radiant heat transfer. This is the purpose.

このため、本考案の構成は、加熱炉のバーナを
設けない予熱帯において、天井との間にガス流を
通す距離を設けたバツフル板と、該天井に密着し
たバツフル板とが、被加熱材の進行方向に交互に
配置された上部バツフル板群を備え、かつ、炉床
との間にガス流を通す距離を設けたバツフル板
と、該炉床に密着したバツフル板とが、被加熱材
の進行方向に交互に配置された下部バツフル板群
を備え、しかも、前記上部バツフル板群の板数が
前記下部バツフル板群の板数よりも多くなつてい
ることを特徴としている。
For this reason, the configuration of the present invention is such that in the preheating zone of the heating furnace where no burner is provided, a buttful plate with a distance between it and the ceiling to allow the gas flow to pass through, and a buttfull plate that is in close contact with the ceiling are connected to the heated material. A group of upper buttful plates are arranged alternately in the direction of movement of the heated material, and the buttful plates are provided with a distance between them and the hearth for gas flow to pass through, and the buttful plates in close contact with the hearth are used to heat the heated material. The present invention is characterized in that it comprises lower baffle plate groups arranged alternately in the traveling direction of the vehicle, and the number of plates in the upper buffle plate group is greater than the number of plates in the lower buffle plate group.

以下、本考案の一実施例について、第3図ない
し第5図を参照しながら説明する。
Hereinafter, one embodiment of the present invention will be described with reference to FIGS. 3 to 5.

第3図および第4図は本考案の一実施例を示し
たもので、同図において、1は予熱帯、2は加熱
帯11からのガス流を示す矢印、3は被加熱材の
スラブ、4はスラブサポートパイプ、5と6は天
井と炉床のそれぞれに設けたバツフル板である。
3 and 4 show an embodiment of the present invention, in which 1 is a preheating zone, 2 is an arrow indicating the gas flow from the heating zone 11, 3 is a slab of the material to be heated, 4 is a slab support pipe, and 5 and 6 are buttful plates installed on the ceiling and hearth, respectively.

すなわち、予熱帯1には、天井および炉床との
間に各別にガス流路mを設けたバツフル板5と、
天井および炉床に各別に密着したバツフル板6
が、スラブ3の進行方向(炉の長手方向)に交互
に、炉幅方向全面に設けられている。
That is, the preheating zone 1 includes a double plate 5 having separate gas passages m between the ceiling and the hearth;
Batchful board 6 that adheres to the ceiling and hearth separately
are provided alternately in the advancing direction of the slab 3 (longitudinal direction of the furnace) over the entire surface in the furnace width direction.

前記バツフル板5と6は、耐熱金属、耐火材、
セラミツクフアイバーがよく、上流側からのガス
ふく射を遮断する材料である。また第4図にみら
れるように、上部のバツフル板5は耐熱金属吊り
棒7で、下部のバツフル板5は耐火材製柱8で支
持されている。
The double plates 5 and 6 are made of heat-resistant metal, fire-resistant material,
Ceramic fiber is a good material to block gas radiation from the upstream side. Further, as shown in FIG. 4, the upper buttful plate 5 is supported by a heat-resistant metal hanging rod 7, and the lower buttful plate 5 is supported by a pillar 8 made of a fire-resistant material.

このように、上下のバツフル板5は、天井およ
び炉床との間に各別にガス流を流す距離mを設
け、天井および炉床の近くのガスを流し出し、上
下のバツフル板6は天井および炉床に各別に密着
して、ガス流をスラブ3に沿わしめて速い速度で
流す。これらガスの流れを矢印2で示している。
また炉床近くの温度の低いガス、とくに天井近く
の温度の低いガスが速く動かされることにより予
熱帯1内のガスが常に高温となり、伝熱が増加
し、バツフル板6の自由端のガス流は高速で流れ
るため対流伝熱が増加する。
In this way, the upper and lower butt-full plates 5 provide a distance m between the ceiling and the hearth for each gas flow to flow out gas near the ceiling and the hearth, and the upper and lower butt-full plates 6 connect to the ceiling and the hearth. The gas flow is caused to flow along the slabs 3 at a high speed, each in close contact with the hearth. The flow of these gases is indicated by arrow 2.
In addition, because the low temperature gas near the hearth, especially the low temperature gas near the ceiling, is moved quickly, the gas in the preheating zone 1 is always at a high temperature, increasing heat transfer, and the gas flow at the free end of the buttful plate 6. flows at high speed, increasing convective heat transfer.

第5図は、横軸に矢印方向にガスの温度をと
り、縦軸に第1図および第3図の予熱帯高さHを
とつたもので、点線9はバツフル板のない従来の
ものの温度分布を示し、実線10は本考案の温度
分布を示す。これは、本考案では、バツフル板5
と6を交互に設けてあるため、ガスが充分に混合
し、ガス塊の径が大きくなり、ふく射伝熱が増加
することを意味している。
In Figure 5, the horizontal axis shows the gas temperature in the direction of the arrow, and the vertical axis shows the height H of the preheating zone shown in Figures 1 and 3.The dotted line 9 indicates the temperature of the conventional type without a full plate. The solid line 10 shows the temperature distribution of the present invention. In the present invention, this is the full plate 5.
and 6 are provided alternately, which means that the gases are sufficiently mixed, the diameter of the gas mass increases, and radiation heat transfer increases.

なお下部ガス流はドラフトで上部に上昇の傾向
があるため、本考案では上部バツフル板群の板数
を下部バツフル板群の板数よりも多くし、第3図
では天井に密着させたバツフル板6が2枚である
のに、炉床に密着させたバツフル板6が1枚とい
うようにし、上部の圧損を下部の圧損より多く
し、上下部のガス流を等分にするようにしてい
る。また予熱帯1の高さHは、1.5〜2.5メートル
位で、高くするほうが効率がよくなるが、2.5メ
ートルを越えると効率の増加率が低下する。さら
に、バツフル板5のガス流を通す距離mは予熱帯
圧力損失とのバランスによるが、一般の使用に
は、バツフル5の高さ方向の長さnの約1/3程度
となる。またバツフル板5と6の間隔lと前記長
さnの関係は、つまり、l/nは1〜3が効率がよ い。
In addition, since the lower gas flow tends to rise to the upper part due to draft, in this invention, the number of plates in the upper buttful plate group is greater than the number of plates in the lower buttfull plate group. Although there are two plates 6, there is only one buttful plate 6 that is in close contact with the hearth, so that the pressure loss in the upper part is greater than the pressure loss in the lower part, and the gas flow in the upper and lower parts is equally divided. . Further, the height H of the preheating zone 1 is about 1.5 to 2.5 meters, and the higher the height, the better the efficiency, but if it exceeds 2.5 meters, the rate of increase in efficiency decreases. Further, the distance m through which the gas flow passes through the baffle plate 5 depends on the balance with the pressure loss in the preheating zone, but in general use, it is approximately 1/3 of the length n of the buffle plate 5 in the height direction. Moreover, the relationship between the distance l between the baffle plates 5 and 6 and the length n is efficient, that is, l/n is 1 to 3.

このように、本考案によれば、一方の上下のバ
ツフル板は天井および炉床との間に各別にガス流
を流す距離を設けて天井および炉床近くのガスを
流し出し、他方の上下のバツフル板は天井および
炉床に各別に密着してガス流を被加熱材に沿わし
めて速い速度で流すため、天井および炉床近くの
温度の低いガスが速く動かされるようになつて予
熱帯内のガスが常に高温となり、伝熱が増加し、
天井および炉床に各別に密着したバツフル板の自
由端のガス流は高速で流れるため、対流伝熱が増
加する。しかも、前記一方のバツフル板と他方の
バツフル板とが被加熱材の進行方向に交互に配置
されているので、ガスは充分に混合し、ガス塊の
径が大きくなり、ふく射伝熱が増加するうえ、天
井および炉床近くの低温ガスが流し出され、高温
ガスが流れ込むようになるため、ふく射伝熱が、
いつそう増加する。とくに、上部バツフル板数を
下部バツフル板数よりも増加させたことにより、
上下ガスの偏流がなくなり、伝熱性が向上する。
As described above, according to the present invention, one of the upper and lower buttful plates is provided with a distance between the ceiling and the hearth to allow the gas flow to flow separately, so that the gas near the ceiling and the hearth is flowed out, and the other upper and lower The buttful plate is in close contact with the ceiling and the hearth separately, allowing the gas flow to flow along the heated material at a high speed, so the low temperature gas near the ceiling and hearth is moved quickly, and the gas inside the preheating zone is moved quickly. The gas is always hot, heat transfer increases,
The gas flow at the free end of the buttful plate, which is in close contact with the ceiling and hearth, respectively, flows at high speed, increasing convective heat transfer. Moreover, since the one baffle plate and the other buffle plate are arranged alternately in the direction of movement of the material to be heated, the gases are sufficiently mixed, the diameter of the gas mass increases, and radiation heat transfer increases. In addition, the low temperature gas near the ceiling and hearth is flushed out, and the high temperature gas flows in, resulting in radiant heat transfer.
When will it increase? In particular, by increasing the number of upper buttfull plates than the number of lower buttfull plates,
Unbalanced flow between the upper and lower gases is eliminated, improving heat transfer.

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

第1図は従来の加熱炉の断面側面図、第2図は
第1図の断面正面図、第3図は本考案の一実施例
を示した断面側面図、第4図は第3図の切断線A
−Aに沿う断面正面図、第5図は予熱帯内のガス
温度分布の説明図である。 1……予熱帯、2……加熱帯からのガスの流れ
を示した矢印、3……被加熱材としてのスラブ、
4……スラブサポートパイプ、5,6……バツフ
ル板、7……バツフル板吊り棒、8……バツフル
板支柱、11……加熱帯。
Fig. 1 is a sectional side view of a conventional heating furnace, Fig. 2 is a sectional front view of Fig. 1, Fig. 3 is a sectional side view showing an embodiment of the present invention, and Fig. 4 is a sectional side view of Fig. 3. Cutting line A
FIG. 5, which is a cross-sectional front view taken along line -A, is an explanatory diagram of the gas temperature distribution in the preheating zone. 1... Preheating zone, 2... Arrow showing the flow of gas from the heating zone, 3... Slab as heated material,
4... Slab support pipe, 5, 6... Bound full board, 7... Bound full board hanging rod, 8... Bound full board support, 11... Heating zone.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] バーナを設けない予熱帯を有する加熱炉におい
て、該予熱帯には、天井との間にガス流を通す距
離を設けたバツフル板と、該天井に密着したバツ
フル板とが、被加熱材の進行方向に交互に配置さ
れた上部バツフル板群を備え、かつ、炉床との間
にガス流を通す距離を設けたバツフル板と、該炉
床に密着したバツフル板とが、被加熱材の進行方
向に交互に配置された下部バツフル板群を備え、
しかも、前記上部バツフル板群の板数が前記下部
バツフル板群の板数よりも多くなつていることを
特徴とする、加熱炉。
In a heating furnace that has a preheating zone without a burner, the preheating zone has a buttful plate with a distance between it and the ceiling to allow the gas flow to pass through, and a buttfull plate that is in close contact with the ceiling to allow the material to be heated to advance. The upper buttle plates are provided with a group of upper buttress plates arranged alternately in the direction, and the buttle plates are provided with a distance between them and the hearth for gas flow to pass through, and the buttle plates that are in close contact with the hearth are arranged to prevent the progress of the material to be heated. Equipped with a group of lower buttful plates arranged alternately in the direction,
Moreover, the heating furnace is characterized in that the number of plates in the upper buff full plate group is greater than the number of plates in the lower buff full plate group.
JP7359082U 1982-05-21 1982-05-21 heating furnace Granted JPS58176957U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7359082U JPS58176957U (en) 1982-05-21 1982-05-21 heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7359082U JPS58176957U (en) 1982-05-21 1982-05-21 heating furnace

Publications (2)

Publication Number Publication Date
JPS58176957U JPS58176957U (en) 1983-11-26
JPH0116763Y2 true JPH0116763Y2 (en) 1989-05-17

Family

ID=30083098

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7359082U Granted JPS58176957U (en) 1982-05-21 1982-05-21 heating furnace

Country Status (1)

Country Link
JP (1) JPS58176957U (en)

Also Published As

Publication number Publication date
JPS58176957U (en) 1983-11-26

Similar Documents

Publication Publication Date Title
US4711298A (en) Heat exchangers molded from refractory material
JPS639002B2 (en)
JPH0116763Y2 (en)
CN104561515B (en) Continuous way bar plate heating stove and heating means thereof
US1943957A (en) Furnace
US4444558A (en) System for heating broadwise-end portions of metal material
US3201219A (en) Glass melting furnace
EP0453696B2 (en) A tunnel kiln
JPS6021385Y2 (en) Heating furnace with radiant tube
JPS6327609B2 (en)
JPH0135897B2 (en)
US1973689A (en) Method of and apparatus for melting glass, etc.
US2126095A (en) Soaking pit and like heating furnace
JPS6036875Y2 (en) heat treatment furnace
JPS6013036Y2 (en) heat treatment furnace
JPS63501975A (en) Melting furnace and reheating furnace
US1895235A (en) Heat recuperating apparatus of the cowper type and a brick for the honeycomb structure
JPH0587449B2 (en)
US1881388A (en) Recuperator for industrial furnaces
JPS6013035Y2 (en) heat treatment furnace
US1928600A (en) Recuperator
US2661198A (en) Furnace end structure
US3907491A (en) Molten metal superheater and method of using the same
US2257392A (en) Regenerative furnace
SU1527275A1 (en) Packing of air-heater of blast furnaces