JPS5953620A - Heating furnace - Google Patents

Heating furnace

Info

Publication number
JPS5953620A
JPS5953620A JP16529082A JP16529082A JPS5953620A JP S5953620 A JPS5953620 A JP S5953620A JP 16529082 A JP16529082 A JP 16529082A JP 16529082 A JP16529082 A JP 16529082A JP S5953620 A JPS5953620 A JP S5953620A
Authority
JP
Japan
Prior art keywords
heating
honeycomb
heat
width
burners
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
JP16529082A
Other languages
Japanese (ja)
Other versions
JPH0375609B2 (en
Inventor
Katsuhiko Kaburagi
鏑木 勝彦
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.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP16529082A priority Critical patent/JPS5953620A/en
Publication of JPS5953620A publication Critical patent/JPS5953620A/en
Publication of JPH0375609B2 publication Critical patent/JPH0375609B2/ja
Granted legal-status Critical Current

Links

Classifications

    • 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
    • C21D9/0006Details, accessories not peculiar to any of the following furnaces

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Tunnel Furnaces (AREA)
  • Gas Burners (AREA)
  • Heat Treatments In General, Especially Conveying And Cooling (AREA)
  • Heat Treatment Of Articles (AREA)

Abstract

PURPOSE:To decrease the thermal loss in a heating furnace and to improve the treatment capacity by quick heating by providing radiation burners provided with porous refractories for preventing backfiring and combustion sections of honeycomb-shaped ceramics on the furnace wall. CONSTITUTION:Plural radiation burners 13 are provided on the ceiling, floor surface and both side faces in the heating section 9 of a heating furnace. The burners 13 are formed of porous refractories 14 for preventing backfiring consisting of such members that allow the permeation of premixed gases therethrough at the propagation speed of flames or above as well as ceramics 15 of a honeycomb shape provided in contact therewith. A cushion member 16, heat insulating material 17 and solid refractories 18 are interposed around the burners 13 to constitute a housing 19 which is mounted to the furnace wall. The housing 19 is communicated by a through-hole 20 with a mixing chamber 21, where a gaseous mixture of fuel and air is blown through the refractories 14 to the ceramics 15 and is burned to heat directly the honeycomb.

Description

【発明の詳細な説明】[Detailed description of the invention]

この発明tよ、)′J1壁にハニカム形状のセラミ、ツ
ク−Cなる燃焼H′11Sである固体加熱源を設けて燃
1’lのNji約於よび匙理1]ヒノJの向−にを図っ
た加;)フトカ−1に嘱目−る。 圧延り程における鋼、ト」の加熱シζは、スラブ等・7
)用刊の」易合は第1図の尿61(方面面図に示す、1
:うに、スラブ(+1かテーブル・[J−ラ(2)の回
転シマ二より移−:jb t′る、ローラハースL)す
連続加熱炉か、斗た丸1]5モ簀俸利σ)、]易音(↓
第2図の+iIiに]4ノ〒ilE面図(・〔=示すよ
う(τ、丸形管俸4+、t(3)かスキューローラ(4
)1−を円周方向に回転しなから移動Jるバレルハ1す
加熱・jγiか多く用いら才り、J戸内で燃オ・1(I
:燃焼さぜ、その燃焼熱て:r1(・[4j)Jを直度
またCま間1)、:に加熱する方法か一般的に行われて
いる。 −1−配別熱炉においては、例えば第1図のバーナ(5
)より生じる火炎(6)からの燃焼熱かスラブ(1)に
伝わるまでの伝熱機:・14としてQよ次の4つかあり
、燃焼すく炎からの幅9.1(Qlol)二火炎から物
体への直接に熱 ・1ノi壁if+−+からの幅q、I(Qr、、) :
火炎ンCより力1j熱されたりノj砧e :fuかfも
の:凸11ノ支1バ;j+i5 ・jJi内カスからの輻1.A、t (Q+ρ:J、y
j内カスτ介した1凸11)”2(へ熱 メ・]、流伝熱(Qr4) :対7j1.による間随臥
熱り記各伝熱1い−の割
With this invention, a solid heating source of a honeycomb-shaped ceramic and a combustion H'11S called Tsuku-C is installed on the wall of J1, and a solid heating source of combustion H'11S is installed on the wall of J1, and it is placed in the direction of In addition, we are looking at Futokar 1. The heating value of steel during the rolling process is 7 for slabs, etc.
) publication is shown in Figure 1, 61 (shown in the direction map,
: Sea urchin, continuous heating furnace with slab (+1 or table/[J-ra (2) rotation stripe 2-: jb t'ru, roller hearth L) or tota-maru 1] 5 moss salary σ) ,] Easy tone (↓
+iIi in Figure 2] 4 no.
) 1- is rotated in the circumferential direction and the barrel is moved.
A commonly used method is to heat r1(・[4j)J directly to C(1), : to generate the heat of combustion. -1- In the distributed heat furnace, for example, the burner (5
) until the combustion heat from the flame (6) is transferred to the slab (1): ・As 14, there are the following four Q, and the width from the combustion flame is 9.1 (Qlol). Width q, I (Qr,,) from the heat directly to the wall if+-+:
Force 1j heated by flame C: fu or f: 11 protrusions, 1 support; j+i5 ・Radius 1. A, t (Q + ρ: J, y
1 convex 11)" 2 (to heat) through the dregs τ in j, flow heat transfer (Qr4): Pair 7 j 1.

【千は第1表に示トダ11き、
1HIJ今てi(’+ Z+ことか知り八でいる・・第
     1     表 ここで注1−11−べき点は、炉内で燃キ・1を直、l
’9 J蒸焼させて加熱するにも拘らず、火炎からの直
接でJ<熱11tは全体の5〜10%にしか過ぎず、!
J1壁かL:戸/)固体1幅則云熱阻の割合か40〜6
0チと最も多くを占めていることである。 一般に、ガスおよび固体の幅14.1にょる(y、: 
p)l、 flt、’ I’−3次式(pにより求めら
れる・ (ン。−・騎;・1帖・A、W/h  ・・・・・・(
1)ここて、QL、:光、熟睡から発する輻f41伝≠
711.i、、i。 A、::光熱諒の衣面債 [ち;:黒体の全幅R11,、(〜1.。 ε、::ガスまたQ、1国体の幅+〕、+ ・キ・Ii
、11常、燃’13’6 火’% K オケルJJ−X
 幅+1.l :4:、 (Ij、+1.2− (1,
/1で固体幅IJ、1に卦ける固体幅」イ、l率u)0
.6〜0.8にくらべて約凭の航゛Cある。<、rYi
つC1,記式■から、表面積、黒体の全’l’M 41
;7iをカスと固体壁足回−とすALば、固体壁の発す
る輻躬云熱:11.はガスの発する幅4.1伝熱鼠にく
らべて約2倍となる。前記第1表に小した)’j3 葉
面からの1711良臥〃〜か全体の40〜60係を占め
る理由y′、I: 、1記によるものであるか、しかし
従来の加熱すJlの場合Qよ燃焼火炎か−1;L i’
、) i壁に(ム熱さノシ、さらに力j壁から被加熱物
に鮒jj)j(−4−るのであり、最t)尺);、jI
壁への(L<熱かがス幅帽−Cある194係−1−この
間の1′/、名!蜂力率、)・低く、ために−2・ノ!
1(1失か・1択めC−大きいという問題かある。 −まl′杜、このように炉啼面への(1<熱かカス輻」
〕、jてありリリif q、l率か小さいためゾJi壁
)111のY!ll’L度か低r台−に抑えらスジ、D
 −ラバー ス5加1d5JJ−1−CはI:350 
゛c程度、バレル型ノJll ?、QS ’lJ’i 
−r’ &’、L L 250〜1. 、(00’Cカ
1.1恨(!l: fl ッている。1611本かL゛
)のpj’、 +t’irf q、lに:1..−イ’
C&よ−fix に、幅11、Iエネルギー′、At’
 &−J、加熱源の絶灯イilA度の・1東に比例4′
−るので、L記ノl1ll <すJi4j、’4面温1
リ−か1.250−] :350°Cのような1氏r>
、’ C1f1、固体幅引率か友Cあっでも全体の幅(
旧エネルギー歌とL−C1i小さいものしか111らA
Lず、従って高温での被加ス)4す〜1勿のb−4’、
 Ull省、′J〜か?−テえず、処理能力の向にを図
る点Cfd1点かあるという問題かある。 最近、例えば連続、νj造装置−(rl;<1琶1し/
c温ハスラフ(、′fり100(1°c)?c、7i気
誘ij;υIf;i’!’Jt:、 、−1: jI1
−+l〔に適した2/i+’を度(1,1,50〜L2
50’C)&・二まで急速加熱をrfい処J、!l!能
力の向1..を図る方法か一部“で行わJシでいる。し
かし、この電気誘導加熱は、誘LF−1コイルの形状に
もよるか一般に、加熱効率か入力′電力比(I<vV/
86(Bj)では40〜70係であり、発電効率を見込
んだIぐ〜へ’/2450−では14〜25係であり、
角力式の加熱効率110〜(50%にくらべて著しく小
、経済゛Cあつこ−その1−設D111費用も嵩むので
、一般的に用いらiシる−まてにに1至つ−こいない。 本発明Q」、かかる現状に鑑み一部なさ八/こもの−C
1従東の加熱た−1における熱損失を1げ反曲に(氏減
し乙燃1’+の頗約を図る々ともに急速加熱ケζよる処
理能力の向J−を図り1(Lる加熱炉の提供を1−1的
表するものCある。 本発明前/Qま1.」ホl−た1Ill′Ii牛1碑′
の大きい固体・19.1伝熱に着11シて、ciLを最
もイj幼(、こ活用したノル熱すJlを開光J−べく利
し々ノ4jり樋ノ(′冗を11(ねた。そのjj’l’
j ’l’L:、力i鳩セにハニカム(QのL10ノ影
、(人のセラミンク(以ドハニカムセラミ゛ツクという
)の内部で燃料を燃焼すせ、ハニカノ・センミンク表面
を1・1,1I((加熱詠とする幅!A、1バーナを設
けること(・′こよって、固体帖洩、1シてよる加熱か
最も自効に活用Jされ従来の問題点をすべて1リイ決し
得ることケ見出し、t。 寸なわち、この加熱・+3−jI:i第1(パσ、多数
の〕火い空間内でハニカムセラミンクを燃焼火炎により
直接加熱J〜るものであるから、火炎と71ニノJムと
の1i’dfciiピ率のよい1jij(伝達か行われ
1、I)(111失ヱ・11ジ(めて少くして固体υ1
j熱諒かrl」1らノシる・第2に、1−記の911く
燃焼火炎と〕\ニカ1、間て1七イニグ)よい熱交換か
f」わノしるため、ハニJ)ムr!it冒すを燃i++
’4.火炎のf:llf度と大差のない(!i!Ll恩
(1600〜180領(: ) t−C加熱し得−℃、
従来J3j−蹄(都度にくらべてイセめC高・品のir
’、1雌加熱源”E I!iることかjり能となる。−
!た1−古己/飄ニノJ)・セラミック内部でのす熱焼
において(lよ、逆火防11−装;1.!’iの設ii
’jか心安と7ダるか、これにメJシ(にl: ”ニカ
ノ、にす然IIとり)で気の混、/1気体を逆火缶1I
L−イCい床用−(1共給−(−きるような多孔質1n
]1火1勿を、:I’l r記ハニノJムの7!I′後
に接して配設rることによ−)こ1′分にメ:1洪4−
ることか°Cきる。 −djノこ1−記ハニカムセラミック内部こ燃(1侘燃
:克させてハニカトセラミソ、りを高幅」A、1熱源と
Vる7′コめの条件どし−Cは、次の、D〜((3)の
k flをi’if’i足するようにハニカムを構成す
ればよいこともl17fi +!、SL、′と・(1)
ハニカム内部燃焼に安する空Krギ>45(14■ ハ
ニカム内1t15燃焼に安する。Itl気速jす゛火炎
1パ涌速度 ’、iJ)  ハ= ’jJ ム内i’tlS燃焼K 
−’19 rル空1r」:j径゛1胴φq]l 、’+
l J:)” % 、、1:’、 Ji己のり11(高
71情の固1本)J旧1J旨原の幅利バーナ全1+if
rえた加1ηJすJlか、健宋Jノjに比較して、イ→
、甜ノJ旧ζノ5カ・1す1指きなるのQ・ユ次の」1
18山から−rある。7.11.11目の加熱(tζお
ける固体加熱源からの1’:+曹、1工不ルキーiff
、’ &−1次式・?)によりシ](め1:、れる、。 こζ−τ゛(Q:輻[」、jエネルギー(1;φ、:加
ブ坊源々jill;fl Hのj田1キ1糸浅(’\v
 :加熱源のto −<”l iMr IQ:1’c 
 ’  、!岡]:4の211色文J’ j!111r
 m11列えばil、lpわし1/j 、:<反の1品
■1ハスラフ゛(1000’C)全ローラハースノ1i
j1.7用許すリ戸で力11)ノ(4−る1易r7、ハ
ニカトセラミックの憎(’1.1バーナを備えだ加#A
 1Jiと従来炉との・1〜・+f 月、Iエネルギー
111を、ハニカム衣用1晶■j実を1.80を丁仏1
i(i東(、)iの力i壁昌曳蛍1:(50゛cとし2
こ、12式l2)(・Cより」七1殴F汁犯+゛l−る
と、ハニノJ 7−% 1iR1j I旧バーナ足11
il′iえたi′Ji!;1. +)t、來jノiのz
、71゛音となる。まだ1列えばr!iA 21i1f
lイ市・(600’c )全バレル型加熱・17−iで
加−l−る場r?、ノ\ニノノム面イ!l11r IQ
i IO20’(:、従来・jプ1壁面(!1111,
1騙125(IcとしてJ七l咬すると、ハニカム幅用
バーナ’a: l1ifiえ/こ・垣は従来りJiの2
.44;:’<、となる。このようにハニカA +h宿
(,1バーブ−を1ノ市えたり月のl’+“if 11
.Iエネルキーi1j’ &:J、’従宋・1月に比較
して2.714〜27倍と人11」に楯”えるの゛(ぞ
ルだけ鋼Hの加熱時間か1JXj、I柄へ7L、1j・
・、11開鴎かζり能と;ダるのである。 本発明に1.I−記知兄に基い°(’/、:=寵シ、′
こもσ)(−1その安旨碍J−るところは、り然オ′1
カスとりと気σ)Jゝ山−音ガスか火炎1八11丘1屯
度以ヒの法度−Cjl 、Ji4 ’J−るよ・)7午
逆火防市川多孔t−111]11火物と、該111j・
1火物と1・1何ノ′;、1−C設ホたノ・ニノJム形
状のセラミンク−(なる燃13″J、部と?I:具備し
た動l、1バーナ蕾カー1壁に−・か、1: (Q A
’(i、閘設けたことを特徴と1−る加?PJ4炉にJ
(+ 7’!、+。 次に添イ・1図面に基いC本発明(/’) )Jl+熱
IJ欧、!; I:、、にiiF細に説明する8 第3図(は本発明を実施l−るスラー)加、で!1.1
11σ) 1.1−ラハース型連、読加熱すノーiノ)
−1シリを・101;[にinr 1+!II jin
図、第4図は・乃:3図の加熱j’iB L” )−世
へ(・1ツノ(小す)の拡大11〆l新側面図、第5図
シま:】5・I IL牡1八、A線の縦断市面図である
。 第3図に示すす11く、炉は図1.右から71−\1l
Ilに4JI熱同収用5(7)と予熱r:13+s)と
加熱部(0)とからl+l′Ji+7さlし、スラフ(
1))よりilに配設さ才゛したチーフル1」−ラt、
1(1) 、1.:。 金、ロールの回転によって・νえ人1−1 (、+ +
)から曲111冒1(1のに向けC水−甲にfflン蓋
さf’Lろ。また第4戻び第5図に示すLllく、加熱
F71S(9>に4s1人井反び床面Q′(1、iJ向
fる複数制の′1xlA +にlバーナ(1艷か、イた
両11111曲にもそノLぞノし対向して複数個の幅l
旧ノ\−すθ;9か、スラフの移動ラインに向けて所定
の間隔で一列げ二1配置さ7′Lでいる。 第6図(f>(ロ)Qよ幅14.1バーナ(1,め+2
) J’j4 J告J)−例を示す、452明図で、(
イ)&、l: *(if:断市曲図、(D) 2:’i
、 Ii(面図−Cアル。 図示例では、中1“jf 、W、lバーナ(jl」そi
L’fニル第2.1@にこ示し/こ部セか1:)なる逆
火防止用1の多孔+77j l制火物(14)と、この
前に接して設け7’j/Xニカムセラミノク(1つと、
こlしもの周囲音iiに I・lil 4’4’ (+
[))、断M (N’C17)および固定1制火物(1
8)を介在さ−11−て堅固にiノ1目j’5U−乙ソ
′11壁に取(・1けるハワンノグQ!jとか1′)構
成さノしZ)。 ]−記多化’Pf、 l制火物の厚さは、;’!’J(
的シ(二定常、グ熱伝導人!沈Ci然・p;+1ノー;
鼾晋則の席冒しか/、゛1火ト11゜;、 101以1
・になる1ギ 一エ lで− 寸だハウシンJ’ (1りは中火に設けたみ孔v(lこ
より燃料と空気とを混合する混合室・鋤に通ししおり、
この晶(〒゛呈(29ンτ開11する燃料カス供給管(
ホ)かCつの燃料と同じく開[−1する送気管@かもの
2気とか混合室・21)で混合して多孔質耐火物(14
)を経てハニカムセラミック0υに吹込まノt、ハニカ
ムセラミックOr)内で燃焼してハニカムを直接加熱す
る。 まだスラブの両側面を加熱する幅η、(バーナ(第5図
に示す)―、該バーナを保i¥rる側壁(ハ)蜘ごと、
スラブ11]に応じて輻射に熱形態1糸数が最大1直勿
r(1ら)しるようにJり変の構造となって計り、各側
壁″2→に取(qけたンリンター(ハ)のロンドい■の
進1尺によっテハーナ吉スラフとの間隔か嫡出に調整さ
ノシる。 テーブルローラ(」0)は、鋼製ロールにセラミックス
(S i N4)スリーブを外押した+l++・I熱性
4′A′)1′−1からなっている。 加熱炉の入1」側には、幅側バーナ03)から排出され
た高温排カスを吸引して、幅利バーナに送る空気との熱
交換を行わしめる排熱回収部(7)か設けられており、
前記高温υ1ガスは前記排熱回収部(7)で熱回収され
、1氏温(約425’C)カスと7”1つて排風(幾1
27)を経て外部に排+1+される。 また、第4図および第5図に小tソ11 (,1110
士部に、U31底に冶って内、413にスケールj蚤き
出しコンベア(281を敷設した水イ・馴すDか設けら
〕tでおり、スラブに発生したスケールか水(:Hl、
lj・29)中に洛1・してコンベア(′2Aで外(小
に(般1若I発棄さlし、抽出スケールの1寺出しf(
\旬、の節減ケ図っている。 次に本発明のうち丸ノ駁・筒棒]」の加熱に適した加熱
J、+iについて「説明する。 第7図シよ/1\光明を実711.!iする丸型者棒(
」川のバレルを加熱・)11例の−;な13疋小す縦1
析IItII lflス、第8図Q↓第7図′?I: 
13− B線で切断して拡大した縦断tlE 1−fl
!図である。 第7図に示すダU<、1反加熱物(′図)」〈例−て゛
は丸形鋼管)か、炉内に+Mj :を嵌に沿って配?没
さytだスキューローラ(ユ」−を円周方向に回・lj
+−t シ/:から矢印、21)の方向に水平移動する
。バレルJJ’iの内接面K kよ進行方向に適当間隔
にW atLのii、li4則バーナ(31〕か配置没
されている。この各幅利バーナ(31)は、iq記と同
7謙に構成さf’しているか、バレル炉1に用いらノt
ているものは第8図に示すダ11く、ハニカム表面を内
1円に向けて円弧状に形成されており、この4閘の輻ψ
1バーナ(31)かすγ1壁面」二に等間隔にす)−1
内に向けて突設した4飼の耐火物(32)に支」・イさ
れて・j11壁而に同心に固定されでいる。1だ図示例
では各輻14.1バーナのハウジング(33)にりま、
前記と同村’(’ (h:中火に透孔(34)か穿設さ
れ、燃゛伺と空気とを混tトツるミキサー(35)から
燃料と空気の’Q (’r気体かそれぞれ導入管ライン
(:(6)を経て前記透rl(34)か1゛7バ一ナ内
部に導入され、多孔Vj、1111f火物(:(7)を
+tD ツー(: セフミックハニカム(38)内で・
燃1al、(ハニカムを直接加熱する。この加熱により
高1111I(となつ/シビラミノクハニカム表面か固
体幅用加熱源と/fっζスキューローラ(ツo) 、、
11を水平移動する姥1市・(3り)全全周囲から加熱
するのである。 次に実施例を掲げて本発明のフカ果1説(り目−る・実
施例 1 第3図に示しン″こローラハース型加熱″i、i”iに
おいて予熱部の長さを5・n、加熱部の手法を長さ1.
0.000+nm×11月500 +++m X高さ4
00)rr蛯し、加!WS :415 fこ発メ、A 
ifi、i =i法かG OOmmX 4 e) O”
 = 0.24− m”の東”ハロ1ノく−ナ全1−ト
山iに40周宛u″80(固(i、 9.2 nio)
、さらに両側Jjiに10個宛#l−2011i111
(4,8n? )合削゛24 n?配、没して1.随さ
8000+t1m X l’l−J l 030+++
mX厚さ210 mm、中。屯]−3,5001(yの
連続、1ZrJ貴〃清片スラフ(L000’C)を1.
11ノ’/3)の5虫j皆です戸内蛍移動させて120
領c−4での加熱1行った。この場合、スラブはL O
8t/+1で)ノー1内をI’i司lAされることにな
り、その加熱に必要な熱昂、は3.!564 X 10
”V、U11となる。また1記幅帽バ・−すからの燃焼
容(flを5(団Xl’Q”kν個、幅・(,1バーナ
の加熱’t!;!、度1800 ’Cとすれば、幅内ハ
・−すから&−J−77:3−レ′r1]′・11・C
の幅ノ4.1伝熱か(B、宿されるとさとなる。 一方、’111’if q−1曲・7’)’ 、l’4
効1酊イ責Uつ&−,J、’ tX代((3)Q = 
(l R・△しIC・・・・・・・・・・・・■で求め
られるからy Q = 3,564. X I 03F
j/l+、旧く・・773KtA/++12・hパC1
△t=(i8oo−iooo)“Cとトれば、式・、蔓
)かしF = 5.8 +nとなる。従って理論的には
輻1]、1バーナの発熱面積は5.8n?となるか、本
実施例では操者の変動、その他外乱を吸収するために約
44?1の24m′と[,2(−い4′21、 その結1]払 ノ、ラフ&qt−i襟ノ5部5Il+、
ノJlハJ〜部t r:、 rll ill 5”’ 
II”II ヲ4″J↓71分でi+T+ 、i、17
aし+ 00 (1’Cか’) l 2 Q () ′
cIII加熱されノしi、r iの〕′−熱部、加熱部
のτ]法を1.記と回る。1;七したに来1)iにおい
て、同11.にスラブ(1)加熱Q?jう1易i’+&
J、約60分の加t?A IL”j間蕾’D ’J’−
A (1)−t’、本発明)31’tでおいてVま加3
・15時間6:約−にτ11縮4−る効果かrllられ
/’j n 本実施例の熱精算金示すと第3表の11〕よりとなる・
錫     3     表 すなわイハ木例ては燃r+にコークス炉ガスを廂宋・ノ
戸と同1手に8401’!n’/I〕テ(史JIJLA
、)−r燃1:[rスの人h・Js (〆よ:3,80
4 X ] 0”)J/ h−Cあった。 第1表(/で−j(ず通り、本発明j〕1にJ=、−げ
る;込効キロ−↓mJ T、:I2にスラブの加熱を1
」゛つ/こ腸ど]の熱動・、l< 、1.」、55%f
あるから、本発明IJjのゑノ5効−4” J、rIt
 、13 i、j iにくらべて45%向」−を小し7
′こ。 ま /ヒ木 ブ邑叩■)ツノ11 □)、ノ(・j)i
シ1、−)廻ノドの ノ11<  ノ刀1改・ノ(jl
、11凸1 の人1]J7伝短)11iかrl、1られ
る7yめ、装置全体の規模の縮少か11j能となり、設
置+iij 行用を人11」にi:iii減し75)る
効果もある。 」菖1′lll11]2 i:f’r 71′A’/C示り、 k 本発明ツバl
/ /l/ ノ%q )III Hlノ(9,1i Q
 用イて、燃4−1とl〜C実施実施例示(〜たと同、
i+にのコークス・j)1カスI、: l’+Il川し
、外径24.4.5 、」1lll X JQさI 2
,500+:unX肉)3J、′l 2+11111の
l晶1痔0(Hl“C1,/)、J1111百足、:i
51/l+の力1陽J(能力?’ I 200°cに加
熱した。−土、′と比11校のため1.i己と同1.1
(−j法〕frt東J、jiテ川用−c、l”I 11
り(1) ;1liiij J:’i’ f 回4..
1゜(・τ別号)(シた・その1゛請宋<11比較しC
’2’+ 4表に小J−8第     4     表 なお本発明i′J−1の幅J〕、1バーナの幅」、1而
l″111.亀か[(幻0”C1従来ゾ戸のバレル内壁
面温度か1250 ’C?2あったので、[山j石′の
中量I、1エネルギ・−ej−蛍Jい佼4−イ3と1角
に述べた式1(4)による1貌で小[刀′こ辿り、4\
7Ir、明j)1の幅用エネルキ−ji’f−1’:J
:従来・カjに比較しC2・1・1陪詰なるので、全伝
熱;τ;−の概略割合の比111シ&、l第5 hIt
(−示す通りとなる。 第5イト− 1、表の7詰果から、木イC明)ノー1における鋼lイ
加熱(・こ閥ノーる炊信し’j、 (1′I、餉jよ2
70×IO’ト「1 と7ケリ、従来リプiの45 (
、) X l O”W/ lに比較し−C約・10茄の
即誠か11,1られだ。 以1.の説明から明らかなように、本発明の加熱J、7
−iυ」2、加熱・j;iと17でセラミックコアーか
らなる幅用バーナを・使j]]シ、彼加熱物への固体幅
口、1伝熱;石。 蛍flit宋がより大11」に増加させだから、熱効率
の向−1書こよる燃(Iの節減および急速加熱による那
理目ヒ刀の向−(、か1り能となったので% iト:”
l ’I”I加熱コストの1氏減に多大の効用缶もたら
すもの−Cある。
[1,000 is shown in Table 1.
1HIJ Now i('+ Z+Knowing 8...Table 1Here, note 1-11-The power point is that the combustion key 1 is directly in the furnace, l
'9 J Despite being heated by steaming, the direct heat from the flame only accounts for 5 to 10% of the total heat!
J1 wall or L: door/) solid 1 width rule yun heat resistance ratio 40~6
This accounted for the largest number of respondents. In general, the width of gases and solids is 14.1 (y,:
p) l, flt, 'I'-Cubic formula (calculated by p.
1) Here, QL: Light, the radiation f41 emanating from deep sleep≠
711. i,,i. A, :: Light and heat ratio's uniform bond [chi;: Full width of black body R11,, (~1.. ε,:: Gas also Q, width of 1 national polity +], + ・Ki・Ii
, 11 always, fire'13'6 fire'% K Okel JJ-X
Width +1. l :4:, (Ij, +1.2- (1,
Solid width IJ is /1, solid width is 1, l ratio u) 0
.. It has about 100 mph C compared to 6-0.8. <, rYi
C1, from the notation ■, the surface area, the total 'l'M of the blackbody 41
; If 7i is the base of the solid wall and the solid wall, then the heat emitted by the solid wall: 11. is about twice the width of the gas emitted by 4.1 heat transfer. (Table 1 above) 'j3 The reason why 1711 good lying from the leaf surface accounts for 40 to 60 sections of the whole y', I: , Is it due to 1, but the conventional heating method If Q is a combustion flame -1; L i'
,) i to the wall (mu heat, and further force j from the wall to the heated object)
To the wall (L< heat shines width hat - C 194 section - 1 - 1' between this /, name! Bee power rate, )・low, for −2・ノ!
1 (missing 1/Choice 1 C-There is a problem of large size. -Mali' Mori, like this, (1 < heat or dust radiation)
], j, if q, l rate is small, zo Ji wall) 111 Y! Lines suppressed to ll'L degrees or low r range, D
-Rubber 5 addition 1d5JJ-1-C is I:350
About ゛c, barrel type Jll? , QS 'lJ'i
-r'&', L L 250~1. , (00'C is 1.1 grudge (!l: fl is on. 1611 lines or L゛) pj', +t'irf q, l: 1..-i'
C&yo-fix, width 11, I energy', At'
&-J, 4' proportional to 1 east of the heating source.
-So, L Note l1ll <su Ji4j, '4 surface temperature 1
1.250°C: 1°C such as 350°C
, 'C1f1, solid width pulling factor or friend C even the overall width (
Old energy song and L-C1i only small ones 111 and A
B-4' of 4s~1m),
Ull Ministry, 'J~? -There is a problem in that there is only one point Cfd to improve the processing capacity. Recently, for example, continuous, νj manufacturing equipment −(rl;
c warm Haslav (,'fri100 (1°c)? c, 7i ki ij; υIf; i'!'Jt:, , -1: jI1
−+l [2/i+' suitable for degree (1, 1, 50 ~ L2
Rf rapid heating up to 50'C) & 2 J,! l! Ability direction 1. .. However, in general, this electric induction heating depends on the shape of the induction LF-1 coil, or the heating efficiency or the input power ratio (I<vV/
In 86 (Bj), it is 40 to 70 sections, and in Igu~he'/2450-, which takes into account power generation efficiency, it is 14 to 25 sections,
The heating efficiency of the angular force type is 110~ (significantly lower than 50%, and the cost is high, so it is not commonly used. In view of the current situation, a portion of the present invention Q has been proposed.
In order to reduce the heat loss in the heating process of 1 (L) by 1 and reduce the heat loss by 1'+, we aim to increase the processing capacity by rapid heating ζ. There is a C that expresses the provision of a heating furnace in 1-1. Before the invention/Q1.
19.1 Heat transfer in large solids 11, ciL is the most heated J-L using this. That jj'l'
j 'l'L:, the honeycomb (L10 shadow of Q) is burnt inside the human ceramic (hereinafter referred to as the honeycomb ceramic), and the surface of the honeycomb is 1.1. , 1I ((Width for heating! A, Providing 1 burner (・'Thus, solid leakage, heating by 1 sheet is most effectively utilized, and all the problems of the conventional method can be solved. In other words, this heating +3-jI:i first (Pσ, many) fire spaces directly heats the honeycomb ceramics by the combustion flame, so the flame and 71 nino Jmu and 1i'dfcii 1jij (transmission is done 1, I) (111 loss ヱ・11 ji (very small and solid υ1
Second, is there a good heat exchange between the combustion flame and the combustion flame described in 1-1? No way! burn it
'4. The temperature of the flame is not much different from 1600 to 180 degrees (1600~180 degrees).
Conventional J3J-hoof (compared to each case, Iseme C high/quality IR
', 1 female heating source 'E I!i or jri function.-
! 1. Furumi/Nino J)・In the heat firing inside the ceramic (l, backfire prevention 11-equipment;
'J or Shin'an and 7 da, or me Jshi (Ni l: "Nikano, Nisuzuru II Tori") and mix of air, /1 gas backfire can 1I
L-iC For flooring-(1 co-supply-(-porous 1n)
] 1 fire 1 course: 7 of I'l rki Hanino Jmu! By placing it next to I', I'm going to do this: 1 H4-
It's cold. - DJ No. 1 - Honeycomb ceramic internal combustion (1. ~(It is also possible to configure the honeycomb so that i'if'i is added to k fl in (3).
Empty Kr for combustion inside the honeycomb
-'19 r empty 1r': j diameter ゛1 cylinder φq]l, '+
l J:)” % ,, 1:', Ji self-nori 11 (high school 71 jyo no koku 1 book) J old 1J Umahara's width profit burner all 1 + if
Compared to Kensong Jnoj, I→
, Sweet No.
There is -r from 18 mountains. 7.11.11th heating (1' from a solid heating source at tζ: + so, 1 k iff
,'&−linear expression・? ) by shi] (me1:, reru,. koζ−τ゛(Q: 輻['', j energy (1; φ,: Kabubo Genzu jill; fl H's j field 1 ki 1 Itoasa ( '\v
:Heating source to −<”l iMr IQ:1'c
',! Oka]: 4 no 211 Shikimon J' j! 111r
m11 row il, lp 1/j, :< 1 item ■ 1 hash ゛ (1000'C) all roller hearths 1i
For j1.7, power 11) no (4-ru1 easy r7, honeycomb ceramic hate ('1.1 equipped with burner) #A
1Ji and conventional furnace ・1~・+f month, I energy 111, 1 crystal for honeycomb coating ■ j fruit 1.80, Ding Buddha 1
i (i east (,) i's power i wall change firefly 1: (50゛c and 2
This, 12 formula l2) (・From C"71 punching F juice criminal +゛l-, Hanino J 7-% 1iR1j I old burner leg 11
il'i got i'Ji! ;1. +) t, z of nij no i
, the sound will be 71°. There's still one row left! iA 21i1f
Ii city, (600'c) full barrel type heating, 17-i heating place r? , No\Ninonomu face! l11r IQ
i IO20'(:, Conventional/jp1 wall (!1111,
1 deception 125 (If you bite J7l as Ic, burner for honeycomb width 'a: l1ifi/ko・gaki is conventionally Ji's 2
.. 44;:'<. In this way, Hanika A + h inn (, 1 barb - is added to 1 no city, l' + “if 11
.. I energy key i1j'&: J, 'Junior Song Dynasty, 2.714 to 27 times compared to January and 11 people's shield 'eruno' (Only the heating time of steel H is 1JXj, 7L to I handle , 1j・
・, 11 Kaoru or ζri-no; Daru. The present invention includes 1. Based on I-Kichi brother
Komo σ) (-1 That cheap J- place is Riren O'1
scum removal and air σ) JゝMountain - sound gas or flame 1811 hill 1 ton degree - Cjl, Ji4 'J-yo.) 7 o'clock reverse fire prevention Ichikawa poro t-111] 11 fireworks and said 111j・
1 Fire and 1.1 What';, 1-C installed hota-ni-no-J M-shaped ceramics (Naru fire 13''J, part and? I: Equipped with an organ, 1 burner bud, car 1 wall ni-・ka, 1: (Q A
'(i, The feature is that a lock is installed in the PJ4 furnace.
(+ 7'!, +. Next, attached A.1 C invention based on the drawing (/')) Jl+Heat IJ Europe,! ; I:, iiF will be explained in detail in 8 Figure 3 (is a slur for implementing the invention), and! 1.1
11σ) 1.1-Lahas type series, reading heating no i no)
-1 series・101;[inr 1+! II jin
Figure, Figure 4 is ・No: Figure 3's heating j'iB L'') - To the world (・1 Horn (small) enlargement 11〆l New side view, Figure 5 Shima:】5・I IL This is a vertical sectional view of the city along line A.
4JI heat transfer 5(7) and preheating r: 13+s) and heating part (0) to l+l'Ji+7 to Il, and slough (
1)) more advanced chifur 1”-rat,
1 (1), 1. :. Gold, by the rotation of the roll, ν person 1-1 (, + +
) to song 111 1 (towards 1 C water - ffl n lid f'L ro. Return to the 4th turn shown in Figure 5, heat F71S (9> to 4s 1 person well warped floor Surface Q' (1, iJ direction f plural system '1
9 or 7'L are arranged in a row 21 at predetermined intervals toward the line of movement of the slough. Fig. 6 (f > (b) Q width 14.1 burner (1, eye + 2
) J'j4 JreportJ) - To give an example, in the 452 bright diagram, (
i) &, l: *(if: Danichikyokuzu, (D) 2:'i
, Ii (front view - C al. In the illustrated example, the middle 1 "jf, W, l burner (jl" soi)
L'f Nil No. 2.1 @ This section / This part section 1:) Porous holes for flashback prevention 1 + 77j l Fire suppression material (14) and provided in front of this 7'j/X Nicum ceramic hole (One and
I・lil 4'4' (+
[)), broken M (N'C17) and fixed 1 fire suppression object (1
8) Interpose -11- and firmly attach it to the wall of i no 1 j'5U-otsu so'11 (・1 ke hawan nog Q!j or 1') and make up Z). ]-Kitaika'Pf, l The thickness of the fire suppression material is ;'! 'J(
Target shi (two steady, heat conductor! Shen Ci Ran・p; +1 no;
Shinnori Shinnori's seat was invaded/゛1 fire 11゜;, 101-1
・In 1 liter, 1 liter (1 liter is a mixing chamber for mixing fuel and air.)
This crystal (〒゛present(29nτopening11) fuel scum supply pipe(
E) or C fuel is mixed in the same open [-1 air pipe @ Kamo 2 gas or mixing chamber 21) and porous refractory (14
) is blown into the honeycomb ceramic 0υ, and it is combusted within the honeycomb ceramic or) to directly heat the honeycomb. Width η, which still heats both sides of the slab (burner (shown in Figure 5)) - the side wall (c) which keeps the burner,
According to the slab 11], the heat form 1 thread count is at most 1 straight r (1 ra) according to the radiation, and the J-shaped structure is measured, and each side wall "2 → The distance from the Tehanaki slough is adjusted by 1 shaku of the length of the rond. It consists of febrile 4'A')1'-1. An exhaust heat recovery section (7) is provided on the inlet side of the heating furnace (7) that sucks high-temperature waste waste discharged from the width side burner 03) and exchanges heat with the air sent to the width side burner 03). and
The high-temperature υ1 gas is heat-recovered in the exhaust heat recovery section (7), and the 1 degree temperature (approximately 425'C) gas and 7"
27) and is exhausted to the outside. In addition, Fig. 4 and Fig. 5 show the small t-sol 11 (,1110
In Shibe, inside the bottom of U31, there is a scale j flea removal conveyor (from 281 laid water A and taming D) at 413, and the scale generated on the slab or water (:Hl,
29), put it on the conveyor ('2A) and put it out (small), and take out 1 part of the extraction scale (
\We are trying to reduce the season. Next, we will explain the heating J and +i suitable for heating round-shaped rods and cylindrical rods of the present invention.
' Heating the river barrel) 11 cases -; 13 small vertical 1
Analysis IItII lfls, Figure 8Q↓Figure 7'? I:
13- Longitudinal section tlE 1-fl cut along line B and enlarged
! It is a diagram. Is the anti-heating material shown in Figure 7 (Figure 7) (example: round steel pipe) or +Mj: placed along the fitting in the furnace? Rotate the skew roller (Y) in the circumferential direction.
+-t Move horizontally from C/: in the direction of arrow 21). WatL's ii and li four-rule burners (31) are arranged at appropriate intervals in the direction of travel on the inscribed surface Kk of barrel JJ'i. If it is not properly constructed or used in the barrel furnace 1.
The honeycomb surface shown in Figure 8 is shaped like an arc with the honeycomb surface facing one circle inward, and the radius of these four locks is ψ.
1 burner (31) γ1 wall surface (spaced equally)-1
It is supported by four refractories (32) that protrude inward and is fixed concentrically to the wall. 1. In the example shown, each radial 14.1 burner housing (33),
The same village as above (h: A through hole (34) is drilled in the medium heat, and the mixer (35) mixes the fuel and air. Introduced into the transparent rl (34) or 1゛7 bunrer through the introduction pipe line (: (6), porous Vj, 1111f fire material (: (7) +tD two (: Cefmic honeycomb (38) At the inner·
1al, (directly heats the honeycomb. This heating causes a heating source for the surface of the honeycomb or the solid width / f ze skew roller (tsuo) ,,
11 is heated from all around it by moving it horizontally. Next, an example will be presented, and the first theory of the present invention will be described. , the length of the heating section is 1.
0.000+nm x November 500 +++m x height 4
00)rr 蛯し、加! WS: 415 f, A
ifi, i = i method or G OOmmX 4 e) O”
= 0.24-m'' east of Holo 1 noku-na all 1-to mountain i for 40 laps u''80 (hard (i, 9.2 nio)
, and 10 pieces to both sides Jji #l-2011i111
(4,8n?) Combined cutting゛24n? After death, 1. Size 8000+t1m X l'l-J l 030+++
m x thickness 210 mm, medium. ton] -3,5001 (continuation of y, 1ZrJ Takashi piece slough (L000'C) 1.
11 no' / 3) 5 insects j everyone, let's move the fireflies in the door 120
Heating 1 was performed in area c-4. In this case, the slab is L O
8t/+1) will be heated inside No. 1, and the excitement required for heating it will be 3. ! 564 x 10
``V, U11. Also, the combustion capacity (fl from the width cap bar) is 5 (group Xl'Q''kν pieces, the width . If C, then within the width H-Skara &-J-77:3-R'r1]'・11・C
Width of 4.1 Heat transfer (B, when it is accommodated, it becomes a hole. On the other hand, '111'if q-1 song 7')', l'4
Effect 1 Intoxication Responsibility U & -, J,' tX ((3) Q =
(l R・△ and IC・・・・・・・・・・・・■ Since it is found, y Q = 3,564. X I 03F
j/l+, old...773KtA/++12・hpa C1
If we add △t=(i8oo-iooo)"C, we get the formula: F = 5.8 +n. Therefore, theoretically, the radius is 1], and the heating area of one burner is 5.8n? In this example, in order to absorb operator fluctuations and other disturbances, the rough & qt-i collar is approximately 44?ノ5 part 5Il+,
ノ Jl は J~ Part tr:, rll ill 5"'
II"II wo4"J↓i+T+ in 71 minutes, i, 17
a + 00 (1'C?') l 2 Q ()'
cIII heated part i, r i]'-heated part, heated part τ] method 1. Rotate with the record. 1; In the seventh day 1) i, same 11. Slab (1) Heating Q? j u1i'+&
J, about 60 minutes extra time? A IL"j interbud 'D 'J'-
A (1) - t', the present invention) at 31't, V plus 3
・15 hours 6: The effect of reducing τ11 to about −4− is reduced/'j n The heat balance of this example is shown in Table 3, 11.
Tin 3 Represents Nawa Iha wood For example, coke oven gas for combustion r+ was 8401' in the same way as the Liang Song and Noto! n'/I〕TE(HISTORY JIJLA
,)-r 1: [r s person h・Js (〆yo: 3,80
4 Heating the slab 1
Heat movement of the small intestine, l<, 1. ”, 55%f
Because there is, the effect of the present invention IJj-4” J, rIt
, 13 i, j 45% smaller than i
'child. Ma / Hiki Bumura ■) Tsuno 11 □), ノ(・j)i
1, -) Mawarinodo no 11 < No sword 1 Kai・No (jl
, 11 convex 1 person 1] J7 transfer short) 11i or rl, 1 is 7y, the scale of the entire device is reduced or 11j function is reduced, and the installation + iij row is reduced to 11 people i:iii 75) It's also effective. "Iris 1'llll11] 2 i:f'r 71'A'/C indicated, k Invention collar l
/ /l/ ノ%q )III Hlノ(9,1i Q
For example, 4-1 and 1-C implementation examples (same as ~,
Coke in i + j) 1 dregs I,: l' + Il river, outer diameter 24.4.5, 1llll x JQsa I 2
, 500+: un
51/l + force 1 yang J (ability?' I heated to 200°c. - soil, ' and ratio 11 for 1. i same as self 1.1
(-j method) frt Higashi J, JI Tekawa -c, l”I 11
ri(1);1liiiij J:'i' f times4. ..
1゜(・τseparate issue) (Sita・Part 1゛Song <11 Compare C
'2' + Table 4 shows the small J-8. Since the temperature of the inner wall of the barrel was 1250'C?2, the equation 1 (4) stated in the equation 1, 1 energy - ej - firefly 4 - 3, A small figure with a sword, 4\
7Ir, light j) 1 width energy key-ji'f-1': J
:Compared to the conventional case, C2・1・1 is packed, so the approximate ratio of total heat transfer;
(It will be as shown. 5th item - 1. From the 7th fruit in the table, the steel is heated in No. 1. j yo 2
70
, )
-iυ'' 2. Heating; i and 17 use a width burner consisting of a ceramic core. The firefly flit was increased to 11" by the Song Dynasty, so the thermal efficiency was increased by 1% due to the reduction in fuel consumption and rapid heating. :”
There is something that can bring great benefits to reducing heating costs by 1 degree.

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

弔1図・汀9+)−東のローラバー、ノ、ノ]1す加″
仇J、) i・/)イ・11C回市曲図、第21”4J
 11. +E :k ツバL/ /L/ zlJ 力
11.′f′j5 iノミ D dif% M iJE
 111図、第3図QJ、木プ11明・/)1.U−ラ
ハース型i!15 iツ1し加熱・l′Jiの一1タリ
宏示J−A11t :す?ll:If曲図、第・1図(
よ第:3図の力1巳)(部の一部を詳:rlll vこ
り、 jニーAII′C11′ri(till lf+
1図、第51a&ヨ第4図のA−A線LJ〕j・1ノi
L/)市面図、第6図(イ)、(ロ)Q、[本発明ソJ
1・Z)ilvイf +i、lバーナの(j′シ青の一
1列1・]、J−,況明ソ[C1(イ)は1:6C断市
而面、(l J)?J底而面、尤7図QI1本発明のバ
ーlレノ11り加え・j5 Jjiの一例の部分縁1す
i llill面図、第8図は第7図の13−・13線
C切断した拡大116曲図−(′あ・:)1.1 :ス
ラソ、2.10:テ・−フッL、 li、I−ラ、;(
:丸形511(令(」、4 、 :((1: スキコー
ーロ・−・ン、り:バーーーノー16:火炎、7:排熱
回収部、8:r・熱部、9:加熱部、11:装入11.
12:抽il冒1、■:3.:n:幅川バーナ、幅用、
:37:多孔質附大物、15:ハニノJムセラミソク、
16:緩両祠、17:断熱i’4’、I8:固定酬火′
吻、19.33:ハウジング、202.−34 : 、
+h化、21:混音猷、22:燃+・1ガス111.給
管、23:送気管、24 : 11111壁、25:ン
リノダー、2 (i : IJソド、27:排風機、2
8:掻出しコンベア、2〇二 水イ告、 32 二 面
]火物、 :35 : ミ ギサー、 :36 :ノj
l入管ライン、39):鋼管 出 幀 人 [1−友金属−1−菜株氏ン旨1代理人j
r理七 生  形  冗  屯第7図 rB 第8図 127− 第  6  図
Funeral map 1, 9+) - east roller bar, ノ, ノ] 1 sumka''
凇J,) i・/)I・11C Ichikyokuzu, No. 21"4J
11. +E :k Tsuba L/ /L/ zlJ Force 11. 'f'j5 i chisel D dif% M iJE
Figure 111, Figure 3 QJ, Wood 11 Akira//) 1. U-Lahas type i! 15 Itsu 1 and heating, l'Ji's 11 Tari Hiroyoshi J-A11t: Su? ll: If song diagram, Figure 1 (
Yo No. 3: Power of Figure 3)
Figure 1, 51a & y A-A line LJ in Figure 4]j・1noi
L/) City map, Figure 6 (a), (b) Q, [This invention
1.Z) ilvif +i, l burna's (j'shi blue one 1 column 1.], J-, situation light so [C1 (i) is 1:6C danshijimen, (l J)? J bottom view, Figure 7 QI1 Bar l Reno 11 addition of the present invention, j5 Partial edge 1 of an example of Jji llill side view, Figure 8 is an enlarged view taken along line 13-13 C of Figure 7 116 pieces - ('A・:) 1.1: Suraso, 2.10: Te-fu L, li, I-La, ;(
:Round 511 Charging 11.
12: Extract 1, ■: 3. :n: Hakawa burner, for width,
:37: Porous attached large fish, 15: Hanino J Musera Misoku,
16: Yuryo shrine, 17: Insulation i'4', I8: Fixed fire'
Proboscis, 19.33: Housing, 202. -34: ,
+h conversion, 21: mixed sound, 22: fuel+・1 gas 111. Supply pipe, 23: Air pipe, 24: 11111 wall, 25: Noder, 2 (i: IJ sod, 27: Exhaust fan, 2
8: Scraping conveyor, 202 water ejection, 32 two sides] Fireworks, :35: Migisa, :36: Noj
l Immigration line, 39): Steel pipe exit person [1-Friends Metal-1-Nabu Mr. 1 representative]
Figure 8 127-Figure 6

Claims (1)

【特許請求の範囲】[Claims] (1)j然オ・]カ又と空気の予混謀ガスか火炎伝播速
度以1−の速度で通過するよう7生逆火防市川多孔v■
1制大物と、該1制大物と連接して設けたハニカム形仄
のセラミックでなる燃・暁部とをlAI+iff した
幅q、jバーナを炉壁に一又Vよ複数1固設けたことを
!待機とする加熱ヅ′J’i +1
(1) Pre-mixing gas and air to pass through at a speed of 1-1 less than the flame propagation speed.
A plurality of burners with a width of q and j, which is equal to lAI + iff, are fixedly installed on the furnace wall in a single or V shape. ! Heating on standby +1
JP16529082A 1982-09-21 1982-09-21 Heating furnace Granted JPS5953620A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16529082A JPS5953620A (en) 1982-09-21 1982-09-21 Heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16529082A JPS5953620A (en) 1982-09-21 1982-09-21 Heating furnace

Publications (2)

Publication Number Publication Date
JPS5953620A true JPS5953620A (en) 1984-03-28
JPH0375609B2 JPH0375609B2 (en) 1991-12-02

Family

ID=15809514

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16529082A Granted JPS5953620A (en) 1982-09-21 1982-09-21 Heating furnace

Country Status (1)

Country Link
JP (1) JPS5953620A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61149092U (en) * 1985-03-07 1986-09-13
JPH11224683A (en) * 1997-11-25 1999-08-17 Sulzer Hexis Ag Fuel cell module with built-in auxiliary heating device and plant equipped with the module
JP2010523926A (en) * 2007-04-03 2010-07-15 エス・エム・エス・ジーマーク・アクチエンゲゼルシャフト Burner arrangement
EP2546593A1 (en) * 2011-07-12 2013-01-16 SMS Concast Italia S.p.A. Device for transferring a metallurgical material
WO2013047183A1 (en) * 2011-09-28 2013-04-04 中外炉工業株式会社 Radiant wall burner unit

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61149092U (en) * 1985-03-07 1986-09-13
JPH11224683A (en) * 1997-11-25 1999-08-17 Sulzer Hexis Ag Fuel cell module with built-in auxiliary heating device and plant equipped with the module
JP2010523926A (en) * 2007-04-03 2010-07-15 エス・エム・エス・ジーマーク・アクチエンゲゼルシャフト Burner arrangement
EP2546593A1 (en) * 2011-07-12 2013-01-16 SMS Concast Italia S.p.A. Device for transferring a metallurgical material
WO2013007533A1 (en) * 2011-07-12 2013-01-17 Sms Concast Italia Spa Device for transferring a metallurgical material
CN103797324A (en) * 2011-07-12 2014-05-14 Sms康卡斯特意大利股份有限公司 Device for transporting metallurgical materials
CN103797324B (en) * 2011-07-12 2016-06-08 Sms康卡斯特意大利股份有限公司 Devices for conveying metallurgical materials
US9551531B2 (en) 2011-07-12 2017-01-24 Sms Concast Italia Spa Device for transferring a metallurgical material
WO2013047183A1 (en) * 2011-09-28 2013-04-04 中外炉工業株式会社 Radiant wall burner unit
CN103765101A (en) * 2011-09-28 2014-04-30 中外炉工业株式会社 Radiant wall burner unit

Also Published As

Publication number Publication date
JPH0375609B2 (en) 1991-12-02

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